DRYING APPLIANCE AND METHOD OF DRYING A PRODUCT

专利摘要:
drying apparatus and method. the present invention relates to a drying or heating apparatus that is capable of independently controlling the temperature of the product being heated (for example, to achieve a desired temperature profile) and the radiation wavelength (for example, to maximize the heat transfer rate). for such purposes, a drying apparatus may be provided with one or more heat sources that are mobile in relation to the product being heated in order to increase or decrease the gap or spacing between the heat source and the product. by adjusting the gap between the product and the heat source, it is possible to control the temperature of the source in such a way as to produce the desired product temperature and radiation wavelength.
公开号:BR112013014459B1
申请号:R112013014459-9
申请日:2011-12-12
公开日:2021-04-27
发明作者:Mark Savarese
申请人:Mark Savarese；
IPC主号:

专利说明:

Cross-Reference to Relative Order
[0001] This application claims the benefit of North American Provisional Application Number 61 / 422,076, filed on December 10, 2010, which is hereby incorporated by reference. Field
[0002] The present invention relates to methods and apparatus for drying a product and more specifically, methods and apparatus for drying a product which is in the form of a liquid or paste to remove moisture from it. Background
[0003] The prior art drying apparatus and methods have been used to dry organic products which are in the form of liquids or semi-liquids such as colloidal solutions and suspensions and the like, these prior art drying apparatus have been used primarily to produce various dry or concentrated food products and food-related products, as well as nutritional supplements and pharmaceuticals. Liquid products are usually first processed in a concentrating apparatus which employs a high-capacity heat source, such as steam or the like, to initially remove a portion of the moisture from the suspension. Then, the concentrated products are often processed in a prior art drying apparatus in order to remove an additional portion of the remaining moisture.
[0004] Various types of prior art drying apparatus have been employed, including spray dryers and freeze dryers. Although spray dryers are known to provide high processing capacity at relatively low production cost, the resulting product quality is known to be relatively low. On the other hand, freeze dryers are known to produce high quality products, but at a relatively high production cost.
[0005] In addition to spray dryers and freeze dryers, various forms of belt dryers have been used. Such prior art drying apparatus generally includes an elongated, substantially flat horizontal belt over which a thin layer of product is spread. The product is usually either in the form of a concentrated liquid or a semi-liquid paste. As the belt slowly rotates, heat is applied to the product from a heat source. Heat is absorbed by the product to cause moisture to evaporate from it. The dry product is then removed from the belt and collected for further processing, or for packaging, or the like.
[0006] A typical prior art apparatus and method is described in U.S. Patent No. 4,631,837 to Mogoon. Referring to Figures 1 and 2 of the '837 patent which are reproduced in the drawings which accompany the present application as Figures 1 and 2 of the prior art, an elongated frame or structure is provided on which an elongated water-proof gutter 10 is supported. . The trough 10 is preferably made of ceramic tile. An insulating layer 12 is provided on the outer surface of the gutter 10. The inner surface of the gutter 10 is covered with a thin sheet of polyethylene 16. Parallel rolls 24, 26 are provided, with a roll being located at each end of the gutter 10 One of the rollers 26 is driven by a motor.
[0007] A water heater 15 and a circulation system, which includes a pump and relative piping, are also provided with the prior art apparatus of the '837 patent. The water heater 15 is configured to heat a water supply 14 just below its boiling point, or slightly less than 100 degrees C. The pump and relative piping system are configured to circulate the water 14 through the chute 10 so that a given minimum water depth is maintained across the entire gutter. In addition, the water heater 15 and the relative circulation system are configured to maintain the water supply within the chute at a temperature which is slightly less than 100 degrees C.
[0008] A flexible sheet of polyester, made of transparent to infrared material 18 in the form of an endless belt is supported around the rollers 24, 26 at each end, and is also supported on top of the water supply 14 within the trough 10 That is, the polyester belt 18 is driven by the roller 26 and rotates around it and the roller 24, while floating on the water 14 inside the trough 10. A thin layer of liquid product 20 is applied over the rotating belt 18 through a product discharge means 28 which is located at an inlet end of the apparatus.
[0009] As the product layer 20 moves along the trough 10 on the belt 18 which floats on the water 14, the product is heated by the water 14 which is kept close to 100 degrees C, and on which the belt 18 floats. The heat from the water 14 extracts the moisture from the product 20 until the product reaches the desired dryness, after which the product is removed from the belt 18. The rate at which the belt 18 moves through the rail 10 can be adjusted so that the product 20 reach its desired dryness at the discharge end of the appliance where it is removed from it.
[00010] Several characteristics of the apparatus and drying method described by the '837 patent lead to an inconvenient and problematic use of the apparatus. For example, trough 10 of a typical prior art apparatus as described by the '837 patent has a length within the range of 12 to 24 meters or more. As a result, the device occupies a relatively large amount of production space. Also, several potential problems relating to the operation of the prior art apparatus can be attributed to the use of water as a source of heat. For example, the prior art apparatus requires a relatively massive heating and water circulation system 15 for its operation. The heating and water circulation system 15 can be problematic in several ways. First, the heating and water circulation system 15 adds complexity to the configuration and construction of the device as well as to its operation. System 15 incorporates a water heater, a pump, and several tubes and valves which all must be kept in a relatively leak-proof manner. The required heating and water circulation system 15 can also impede the ease of mobility of the prior art dryer due to the bulky nature of the system and due to the need for a water supply.
[00011] Secondly, water 14, which is kept below the boiling point, can serve as a port for potentially dangerous microbial organisms which can cause contamination of the product 20. Thirdly, the presence of a large amount of water 14 can serve to be against the purpose of the prior art apparatus which is to remove moisture from the product 20. That is, the water 14, through inevitable leaks and evaporation from the trough 10 can enter the product 20 thereby increasing the time of drying of the product.
[00012] Furthermore, as water 14 is the only source of heat for drying product 20, and as the water temperature is kept below 100 degrees C, the drying process for product 20 is relatively slow. As a universally accepted rule, the amount of heat transferred between two bodies is proportional to the difference in temperature of each body. Also, as a general rule, the moisture contained in the product to be dried must absorb a relatively large amount of energy in order to vaporize. The product 20 initially contains a relatively high amount of moisture when it is initially spread over the support surface 18. Thus, a relatively high amount of thermal energy is required to vaporize the moisture and remove it from the product 18.
[00013] However, as the temperature of the water heat source of the prior art apparatus never exceeds 100 degrees C, the difference in the temperatures of the heat source and product 20 is limited which, in turn, limits the transfer heat to the product. As the product 20 absorbs heat from the heat source, the temperature of the product will increase. This increase in temperature of the product as it travels through the device results in an even lower temperature difference between the product 20 and the heat source which, in turn, further reduces the amount of heat transfer from the heat source for the product. For this reason, the prior art apparatus often requires extended processing times in order to satisfactorily remove moisture from the product 20.
[00014] Also, the prior art apparatus and method of the '837 patent does not provide any flexibility in processing temperatures because the temperature of the heat source cannot be easily changed, perhaps in any way. For example, the production of some products can benefit from specific temperature profiles during the drying process. The "temperature profile" of a product refers to the temperature of the product as a function of the time elapsed from the drying process. However, as the temperature of the heat source of the prior art apparatus is only limited to 100 degrees Celsius, but also slow to change, the temperature profile of the product cannot be easily controlled, or changed.
[00015] As the prior art apparatus described by the '837 patent uses water as a heat source, and requires a large water heating system for its operation, the resulting prior art apparatus is large, heavy, immobile, complex, difficult to maintain, and can be a source of microbial contamination of the product. In addition, as the temperature of the water heat source used by the prior art method and apparatus is limited to less than 100 degrees Celsius, the drying method of the prior art can be slow and inefficient, and does not provide a modification or close control of the product's temperature profile.
[00016] Drying systems incorporating infrared heating elements can solve many of the problems of the prior art apparatus of the '837 patent. Such a drying system is described in U.S. Patent Number 6,539,645, which is incorporated herein by reference.
[00017] It is known that the wavelength band emitted from an infrared heater can be controlled by adjusting the temperature of the infrared heater. Increasing the temperature of an infrared heater will produce radiation of shorter wavelengths while decreasing the temperature of an infrared heater will produce radiation of longer wavelengths. Previous techniques for heating certain substances with infrared radiation included selecting a specific wavelength band of infrared radiation that is more efficiently absorbed by the substance being heated and / or that produces a desired heating effect.
[00018] U.S. Patent Number 5,382,411, for example, describes an infrared heating system for heating baked goods. The '411 patent describes that known IR food processes control the source temperature of the heaters to adjust the radiation wavelength during the roasting process. If greater surface heating is required, the source temperature is lowered to produce longer wavelengths that are less able to penetrate the product's surface. Conversely, if less surface heating is required, the source temperature is increased to produce wavelengths that are better able to penetrate the product's surface.
[00019] U.S. Patent Number 5,974,688 describes an infrared heating system for drying sludge from wastewater. The system described in the '688 patent apparently maintains the source temperature of infrared heaters at a temperature that produces wavelengths in a range that maximizes the rate of heat transfer to the waste water sludge, thereby minimizing drying time .
[00020] However, the prior techniques of the '411 and' 688 patents are insufficient for heating and drying applications where it is desirable to precisely control the temperature of the product being dried, for example, heating the product according to a profile of predetermined temperature that produces the best results for a specific product, such as drying liquid food products. The need to maintain or control the temperature of the product being dried is directly opposed to the need to heat the product with radiation of a specific wavelength, in order to maximize the rate of heat transfer. For example, if the product becomes too hot, then the heater temperature must be lowered to avoid overheating and / or burning the product, however, decreasing the temperature will increase the radiation wavelength. Conversely, if the product requires more heat in a short amount of time to avoid overheating the product, then the temperature of the heater must be increased, which will decrease the radiation wavelength. As can be appreciated, the prior art of the '411 and' 688 patents sacrifices the ability to control the temperature profile of the product by keeping the heat sources at predetermined settings to produce radiant heat at the desired wavelength. summary
[00021] According to one aspect, the present description refers to a drying or heating device that is capable of independently controlling the temperature of the product being heated (for example, to achieve a desired temperature profile) and the radiation wavelength (for example, to maximize the heat transfer rate). For such purposes, a drying apparatus may be provided with one or more heat sources that are mobile in relation to the product being heated in order to increase or decrease the gap or spacing between the heat source and the product. By adjusting the gap between the product and the heat source, it is possible to control the temperature of the source in such a way that it produces the desired product temperature and radiation wavelength.
[00022] For example, if a specific drying profile requires that the product temperature remains substantially constant through one or more control zones, then the product is typically subjected to less heat in each successive control zone. To maintain the desired product temperature and radiation wavelength, heaters in a control zone can be moved further away from the product to decrease the heat applied to the product while maintaining the source temperature to produce radiation at the wavelength. wanted. If desired, the source temperature and heater positions can be controlled to produce a predetermined constant wavelength in successive zones and heat the product to the desired temperature profile to compensate for changes in energy required to evaporate moisture according to the content of moisture in the product decreases as it dries through each of the zones. In other words, unlike the '411 and' 688 patents, the drying apparatus of the present description has the ability to heat a product or object at a predetermined wavelength, in order to maximize the heat absorption by the product or object, without sacrificing control over the temperature profile of the product or object being heated.
[00023] In a representative embodiment, a drying apparatus comprises a mobile product carrier that has a product support surface for supporting a product to be dried, at least a first and a second heater support, and a controller. Each heater support supports one or more dry radiant heating elements and is movable with respect to each other and with respect to the conveyor to adjust the distance between each heater support and the conveyor. The product carrier is configured to move with respect to the first and second heater supports so that the product supported on the carrier is successively heated by the heating elements of the first heater support and the heating elements of the second heater support. The controller is configured to adjust the temperature of the heating elements of each heater support and the distance between the heating elements of each heater support and the conveyor so that the heating elements emit radiant heat at a predetermined wavelength and heat the product according to a predetermined product temperature profile.
[00024] In another representative embodiment, a drying apparatus comprises a mobile product carrier that has a product support surface for supporting a product to be dried, at least a first and a second heating zone, and a controller. The conveyor is operable to transport the product through the heating zones. The first heating zone comprises a first set of one or more radiant heating elements mounted under the product support surface for an upward and downward movement relative to the product support surface. The second heating zone comprises a second set of one or more radiant heating elements mounted under the product support surface for upward and downward movement relative to the product support surface. The controller is configured to continuously monitor the wavelength of the heating elements in each zone and the product temperature in each zone and adjust the temperature of the heating elements in each zone and the distance between the heating elements in each zone and the conveyor so that the heating elements emit radiant heat at a predetermined wavelength in each zone and heat the product according to a predetermined product temperature profile.
[00025] In another representative embodiment, a method of drying a product which comprises applying a product to be dried on a product carrier surface of a mobile conveyor; transporting the product on the conveyor through at least a first heating zone and a second heating zone; and heating the product with a first set of one or more dry radiant heating elements in the first heating zone and heating the product with a second set of one or more dry radiant heating elements in the second heating zone. As the conveyor transports the product through the first and second heating zones, the temperature of the heating elements and the distance between each set of heating elements and the product support surface are adjusted to heat the product to a profile temperature and cause the heating elements to emit radiant heat at a predetermined wavelength.
[00026] The above and other features and advantages of the invention will become more apparent from the following detailed description, which proceeds with reference to the accompanying figures. Brief Description of Drawings
[00027] Figure 1 is a diagram on the side elevation of a prior art device.
[00028] Figure 1 is a partial view of the prior art apparatus shown in Figure 1.
[00029] Figure 3 is a diagram on the side elevation of an apparatus according to a first embodiment of the present description.
[00030] Figure 3A is a diagram on the side elevation of an apparatus according to a second modality.
[00031] Figure 3B is a diagram on the side elevation of an apparatus according to a third modality.
[00032] Figure 3C is a top plan view of an apparatus according to a fourth embodiment.
[00033] Figure 3D is a diagram in side elevation of a fifth modality that shows an alternative operational control scheme for the device shown in Figure 3.
[00034] Figure 4 is a diagram on the side elevation of an apparatus according to a sixth modality.
[00035] Figure 5 is a schematic diagram showing a possible configuration of communication connections between the various components of the device shown in Figure 4.
[00036] Figure 6 is a diagram on the side elevation of an apparatus according to an eighth modality.
[00037] Figure 7 is a diagram in schematic side elevation, enlarged from one of the mobile heater supports of the device shown in Figure 6.
[00038] Figure 8 is a flow chart illustrating a method for operating the drying apparatus shown in Figure 6.
[00039] Figure 9 is a schematic view, in perspective, of a mobile heater support according to another embodiment.
[00040] Figure 10 is a line graph showing the relationship between the operating temperature of a quartz heating element and the peak wavelength of infrared radiation emitted by the heating element.
[00041] Figure 11 is a graph showing the absorption of electromagnetic radiation by water over a range of wavelengths.
[00042] Figures 12-14 show the temperature of the heating elements in each zone of a dryer under different operating conditions to dehydrate a beet juice concentrate.
[00043] Figure 15 shows the wavelength of infrared radiation in each zone of a dryer under different operating conditions to dehydrate a beet juice concentrate.
[00044] Figures 16-20 show the temperature of the heating elements in each zone of a dryer under different operating conditions to dehydrate a mixture of fruit puree.
[00045] Figure 21 shows the wavelength of infrared radiation in each zone of a dryer under different operating conditions to dehydrate a mixture of fruit puree.
[00046] Figure 22 is a schematic illustration of a drying device, according to another modality. Detailed Description
[00047] The present description provides methods and apparatus for drying a product that contains moisture. The apparatus generally includes a support surface which is substantially transparent to radiant heat. The product is supported on a first side of the support surface or conveyor while the radiant heat is directed towards a second side of the support surface to heat the product for drying. The apparatus may also generally include a sensor which is configured to detect and measure at least one characteristic of the product, such as temperature or moisture content. The measurement of the product characteristic can be used to regulate the temperature of the heat source in order to radiate a desired amount of heat to the product.
[00048] The drying methods and apparatus described here are specifically useful for dehydrating vegetable liquids or liquids (such as juices, purées, pulps, extracts, etc.) and other vegetable materials. Such substances can be dehydrated to a moisture content below 5%, typically approximately 3.0%, while substantially preserving total nutrition and flavor. Due to the extremely low moisture content, dehydrated liquids (or other dehydrated products) can be ground into free-flowing, shelf-stable powders. Powders can be used in a variety of food, nutraceutical and pharmaceutical products. Drying Apparatus Modalities
[00049] Referring to Figure 3, a side elevation view of a basic drying apparatus 100 according to a first embodiment of the present description is shown. The drying apparatus 100 is generally configured to remove a given amount of moisture from a "P" product to dry or concentrate the product. The "P" product can be any one of a number of types, including aqueous colloidal suspensions, or the like, which can be in the form of a liquid or paste, and from which moisture must be removed there by heating. The product "P" is generally spread, or otherwise placed, over the apparatus 100 for drying. Once the product "P" has reached the desired dryness it is then removed from the apparatus 100.
[00050] The apparatus comprises a support surface 110 over which the product "P" is placed for drying. The support surface 110 has a first side 111 which is configured to support a layer of product "P" on it as shown. The support surface also has a second side 112 which is opposite the first side 111. Preferably the first side 111 is substantially flat and supported in a substantially horizontal manner so that, in the case of a liquid "P" product, a its substantially uniform layer is formed on the first side. In addition, lips 115 can be formed on the edges of the support surface 110 for the purpose of preventing product "P" from running off the first side 111 of the support surface.
[00051] The support surface 110 can be configured as a substantially rigid or similar tray as shown. However, in an alternative embodiment of the present invention which is not shown, the support surface 110 can be a flexible, relatively thin sheet which is supported by a suitable or similar support system. The support surface 110 is configured to allow radiant heat to pass through it from the second side 112 to the first side 111. The term "radiant heat" means the thermal energy which is transmitted from one body to another by the generally known process as radiation, as differentiated from the transmission of heat from one body to another by the processes generally known as conduction and convection.
[00052] The support surface 110 is made of a material which is substantially transparent to radiant heat and also capable of withstanding temperatures up to 148.8 degrees Celsius (300 degrees Fahrenheit). Preferably, the support surface 110 is made of a material that comprises a plastic. The term "plastic" means any one of several non-metallic compounds synthetically produced, usually from organic compounds by polymerization, and which can be molded into various forms and hardened, or formed into flexible sheets or films.
[00053] More preferably, the support surface 110 is manufactured from a material selected from the group consisting of acrylic and polyester, such materials, when used in the manufacture of a support surface 110, are known to have radiation transmitting properties. thermal elements for use in the present invention. In addition, plastic resins can be formed on a uniform flexible sheet, or on a seamless endless belt, which can provide additional benefits.
[00054] Also, such materials are known to provide a smooth surface for uniform product distribution, a low coefficient of static friction between the support surface 110 and the product "P" supported on it, flexibility, and relatively high temperature resistance tall. In addition, such materials are substantially transparent to radiant heat, have relatively high tensile strengths, and are relatively economical and easily obtained.
[00055] The apparatus 100 may also comprise a chassis 120. The chassis is preferably rigidly constructed and may include a set of legs 122 which are configured to rest on a floor 101 or another suitable foundation, although the legs may also be configured to support on bare or similar ground. The chassis 120 may also include a support 124, or the like, which is configured to support a dry radiant heat source 130 which is exposed to the second side 112 of the support surface 110. The term "exposed to" means positioned so that a path, either direct or indirect, can be established for the transmission of radiant heat energy, wave energy, or electromagnetic energy between two or more bodies. The heat source 130 is configured to direct radiant heat "H" through a gap "G" and towards the second side 112 of the support surface 110.
[00056] The term "dry radiant heat source" means a device which is configured to produce and emit radiant heat, as well as direct the radiant heat through a gap to another body, without incorporating or using any heating means liquid or substance of any kind, including water. The term "slack" means a space which separates two bodies between which the heat is transferred substantially by radiation and in which the two bodies do not contact each other.
[00057] As the apparatus 100 does not use water, or other liquid, as a heating source or heating medium, the apparatus 100 is greatly simplified in relation to the prior art apparatus which employs a liquid heating medium. In addition, the absence of a liquid heating medium in the apparatus 100 provides additional benefits.
[00058] For example, the absence of a water heating means decreases the probability of microbial contamination of the product "P" as well as the probability of removing the product. Furthermore, the absence of liquid heating medium and associated heating / pumping system allows the apparatus 100 to be moved and configured relatively easily and quickly which can provide benefits in such applications as on-site harvesting / processing.
[00059] The dry radiant heat source 130 is preferably configured to direct the radiant heat "H" towards the second side 112 of the support surface 110. Preferably, the dry radiant heat source 130 is positioned relative to the surface support 110 so that its second side 112 is directly exposed to the radiant heat source. However, in an alternative embodiment of the present invention which is not shown, reflectors or the like can be used to direct the radiant heat "H" from the radiant heat source 130 to the second side 112 of the support surface 110. Also, despite it is preferable that the heat source 130 is positioned so as to direct heat "H" towards the second side 112, it is understood that the heat source can be positioned so as to direct heat towards the first side 111, and so directly on the product "P" according to other alternative embodiments of the present invention which are not shown.
[00060] Preferably, the radiant heat source 130 is configured to operate using either electrical energy or gas. The term "gas" means any form of fuel which may include organic or petroleum-based products or by-products which are either in a gaseous or liquid form. Most preferably, the radiant heat source 130 is selected from the group consisting of gas radiant heaters, and electric heaters. The term "gas radiant heaters" means devices which produce substantially radiant heat by combustion of gas. The term "electric radiant heaters" means devices which produce substantially radiant heat by consuming electrical current. Various forms of such heaters are known in the art. The use of such heaters as the heat source 130 can be advantageous due to the various benefits associated with them.
[00061] For example, such heaters can reach high temperatures and can produce large amounts of radiant heat energy. Such heaters can reach temperatures of at least 100 degrees Celsius and can reach temperatures significantly above 100 degrees Celsius. The high temperatures attainable by these heaters can be beneficial in producing large amounts of thermal energy. In addition, the temperature of the heater, and thus the amount of radiant heat energy produced, can be changed relatively quickly and can be easily regulated by its proportional modulation. Also, such heaters generally tend to be relatively light in weight compared to other heat sources, and are generally resistant to shock and vibration.
[00062] As electric radiant heaters such as quartz heaters and ceramic heaters consume electricity for operation, such heaters can be operated either from a portable generator or from a permanent electric grid. Similarly, gas heaters can be operated either from a portable gas supply, such as a liquefied natural gas tank, or from a gas distribution system such as an underground piping system. Furthermore, heaters such as those discussed above are generally known to provide a long and reliable service life and can be easily maintained.
[00063] The radiant heat source 130 is preferably configured to reach a temperature greater than 100 degrees Celsius, and more preferably, the heat source is configured to reach a temperature significantly greater than 100 degrees Celsius, such as 150 degrees Centigrade. The radiant heat source 130 can be configured to vary the amount of radiant heat that is directed to the support surface 110. That is, the radiant heat source can be configured to modulate the amount of heat that it directs to the support surface. support 110.
[00064] Preferably, the radiant heat source 130 can be configured modulated so that its temperature can be increased or decreased in a fast way. The heat source 130 can be configured to modular using an "on / off" control scheme. Preferably, however, the heat source can be configured to modulate employing a true proportional control scheme.
[00065] To facilitate operational control of the heat source 130, the apparatus 100 may include a control device 131 which is connected to the heat source. The control device 131 can be an electrical relay as in the case of an electrically powered heat source 130. Alternatively, the control device 131 can be a servovalve as in the case of a gas-powered heat source 130.
[00066] The support surface 110 can be configured to be movable with respect to the radiant heat source 130. For example, the support surface 110 can be configured as a movable tray which can be placed on top of, and removed from, the chassis 120 as shown in Figure 3. In an alternative embodiment of the first embodiment of the invention, chassis 120 may include rollers or the like on which the support surface 110 can be supported and moved.
[00067] For example, referring to Figure 3A a diagram in side elevation is shown of an apparatus 100A according to a second embodiment of the present invention. As is evident, the support surface 110A of the apparatus 100A is configured as an endless belt comprising a flexible sheet supported by rollers 123. The support surface 110A can be configured to move, or circular, in the "D" direction.
[00068] The rollers 123 are, in turn, supported by the chassis 120A which also supports at least one heat source 130. The heat source 130 is configured to direct the radiant heat "H" in the direction of the second side 112 of the support surface 110A. Opposite the second side 112, is the first side 111 of the support surface 110A which is configured to support the product "P" on it. As seen, the device configuration 100A can provide continuous processing of the product "P".
[00069] Now looking at Figure 3B, a diagram in side elevation is shown which shows an apparatus 100B according to a third embodiment of the present invention which is similar to the apparatus 100A discussed above for Figure 3A. However, the support surface 110B of the apparatus 100B is not only configured as an endless belt, but also comprises a plurality of rigid connections 113 which are connected hinged to one another in a chain-like manner.
[00070] As shown, apparatus 100B comprises a chassis 120 which supports rotating rollers 123 on it. The rollers 123 in turn support the support surface 110B on top of them, which can be configured to move, or to circulate, in the "D" direction. Chassis 120 also supports a heat source 130 over which it is configured to direct radiant heat "H" towards the second side 112 of the support surface 110B. The support surface 110B is configured to support the product "P" on the first side 111 which is opposite to the second side 112.
[00071] Moving Figure 3C, a top plan view is shown of an apparatus 100C according to a fourth embodiment of the present invention. According to the apparatus 100C, the support surface 110C is substantially configured as a flat, horizontal ring which is configured to rotate in the "R" direction. The support surface 110C can be configured to rotate in the "R" direction around a central portion 114 which can comprise a bearing (not shown) or the like. The upper side, or first, 111 of the support surface 110C is configured to support the product "P" on it.
[00072] The product "P" can be placed on the first side 111 of the support surface 110C in an application station 140, and can be removed from the support surface in a removal station 142. At least one heat source (not shown) can be positioned under the support surface 110C so that the radiant heat (not shown) is directed from the heat source to a lower side, or second (not shown), which is opposite the first side 111.
[00073] Now returning to Figure 3, the apparatus 100 may comprise a controller 150 such as a digital processor or the like for executing operational commands. The controller may be in communication with the radiant heat source 130 via the control device 131 as well as at least one communication connection 151. The communication connection 151 may include a wired or wireless communication means. The term "in communication with" means capable of sending or receiving data or commands in the form of signals which are passed through the communication connection 151.
[00074] The apparatus 100 can also comprise a sensor 160 which can be supported by a ceiling 102 or other suitable support, and which can be in communication with the controller 150 through a communication connection 151. The sensor 160 is configured to detect and measure at least one characteristic of at least a portion of the "P" product. The characteristic can include, for example, the temperature of the product "P", the moisture content of the product, or the chemical composition of the product. Sensor 160 can be any one of a number of sensor types which are known in the art. Preferably, sensor 160 is either an infrared detector, or a bimetallic sensor.
[00075] The apparatus 100 may further include an operator interface 170 which is in communication with the controller 150 and which is configured to allow an operator to enter commands or data into the controller 150 by means of a keyboard or the like 172 which may be included in the operator interface. The operator interface 170 may also be configured to communicate information regarding the operation of the apparatus 100 to the operator via a display screen or the like 171 which may also be included in the operator interface. The controller may include an algorithm 153 which may be configured to automatically perform several steps in the operation of the apparatus 100. The controller 150 may further include a readable memory 155 such as a digital memory or the like for storing the data.
[00076] During the operation of the apparatus 100, the product "P" can be placed on the first side 111 of the support surface 110. Various means for placing the product "P" on the first side 111 can be employed, including spraying, drip, leak, and the like. The operator of the device 100 can enter various data and commands for the controller 150 via operator interface 170. These data and commands entered by the operator can include the product type "P" to be processed, the temperature profile to be maintained on the product, as well as "start" and "stop" commands.
[00077] Algorithm 153 can include at least one predetermined heat curve which is associated with at least one specific "P" product. The term "heat curve" means a location of values associated with the amount of heat produced by the heat source 130 and whose location of values is a function of elapsed time. After the operator identifies the specific product "P" and inserts it in the controller 150, the drying process, according to the temperature parameters dictated by the predetermined heat profile, can be carried out automatically. In addition, the drying process can be adjusted "dynamically" based on inputs from sensor 160 received by the controller during the process, as described below.
[00078] Once the drying operation begins, the sensor 160 can detect and measure at least one characteristic of at least a portion of the product "P" such as temperature, moisture content, or its chemical composition. Sensor 160 may be instructed by controller 150, or otherwise configured, to repeatedly perform the detection and measurement of a product characteristic "P" at given intervals during the operation of apparatus 100. Alternatively, sensor 160 may be configured to continuously detect and measure the characteristic during the operation of the device 100.
[00079] The measured characteristic which is detected and measured by sensor 160 can be converted into a signal, such as a digital signal, and can then be transmitted to controller 150 via one of the communication connections 151. Controller 150 it can then receive the signal sent by sensor 160, and can then store the signal as readable data in readable memory 155. Controller 150 can then cause algorithm 153 to be activated, where the algorithm can access data in readable memory 155 and then use the data to initiate an automatic operating command.
[00080] For example, controller 150 can use the signal data sent by sensor 150 to control the radiant heat source 130. That is, controller 150 can use the signal data from sensor 160 to control the amount of radiant energy "H" directed to the support surface 110. This can be done in several ways such as turning the heat source on or off for specific time intervals, or proportionally modulating the heat output produced by the power source 130.
[00081] In a typical drying operation, for example, a product "P" can be placed on the first side 111 of the support surface 110 as shown so as to be supported on it. The operator can, through the interface 170, communicate to the controller 150 the type of product "P" which must be dried. Alternatively, the operator can enter other data such as the estimated moisture content, or similar, of the product "P". The operator can also have the apparatus 100 initiate a drying operation by inserting a "start" command at interface 170.
[00082] When the drying operation begins, the sensor 160 can detect and measure a characteristic of the product "P" such as temperature, moisture content, or its chemical composition. Sensor 160 can then convert the characteristic measurement to a signal and then send the signal to controller 150. For example, if the measured characteristic is the product temperature, then the sensor can send a signal to controller 150 which contains the product temperature data.
[00083] The controller 150 can then use the data sent by the sensor 160 to regulate various functions of the device 100. That is, the controller 150 can regulate the amount of radiant heat "H" produced by the radiant heat source 130 and directed to the product "P" as a function of the characteristic detected and measured by sensor 160.
[00084] The controller 150 can also regulate the amount of radiant heat "H" produced by the radiant heater 130 as a function of elapsed time, as well as the specific type of product "P" which must be dried. In alternative modes such as those described above for Figures 3A, 3B, and 3C, where the support surface 110 is configured to move the product "P" through the heat source 130, the controller 150 can regulate the speed at which the support surface 110, and thus the product, moves past the heat source.
[00085] The specific type of product "P" to be dried can have an optimal profile associated with it, which, when adhered, can optimize a given production result such as the minimum drying time, or the maximum quality of the product. "P" product. The term "profile" means a location of values for one or more product characteristics measured as a function of elapsed time. For example, a given product "P" may have associated it with a given optimal temperature profile, an optimal moisture content profile, or an optimal chemical composition profile. The readable memory 155 can store the optimal profiles for different types of "P" products. Each of the optimal stored profiles can then be accessed by algorithm 153 according to the instructions or commands entered in the controller 150 by the operator.
[00086] For example, the specific product "P" to be dried, for example, can have an optimal temperature profile that dictates an increase in the product's temperature at a maximum possible rate and at a temperature of 100 degrees Centigrade. The optimal temperature profile can additionally dictate that, once the product "P" reaches a temperature of 100 degrees Celsius, the temperature of the product must be maintained at 100 degrees Celsius for a time elapsed of five minutes, after which the temperature of product "P" should decrease at a substantially constant rate to room temperature over a period of ten minutes.
[00087] The algorithm 153 can try to maintain the real temperature in the product "P" in order to substantially coincide with the optimal temperature profile stored in the given temperature profile of the product "P" by regulating the amount of heat energy "H" produced by the heat source 130. For example, in order to cause the temperature of the product "P" to rise rapidly so as to substantially coincide with the optimal temperature profile, algorithm 153 may cause the radiant heat source 130 initially produce a maximum radiant heat output "H". This can be achieved by causing the temperature of the heat source to rise rapidly to a relatively high level.
[00088] The heat energy "H" is directed from the heat source 130 to the second side 112 of the support surface 110. As the support surface 110 is configured to allow radiant heat "H" to pass through it, the product "P" will absorb at least a portion of the radiant heat. The absorption of heat energy "H" by the product "P" results in an increased temperature of the product which, in turn, promotes the evaporation of moisture from the product. When sensor 160 detects that the product "P" has reached a given temperature, such as 100 degrees Celsius, algorithm 153 can then start a first countdown of elapsed time that has a given duration, such as five minutes.
[00089] During the first countdown, algorithm 153, together with the temperature measurements received from sensor 160, can regulate the amount of heat output "H" produced by the radiant heat source 130 in order to maintain the temperature of the product "P" at a given temperature, such as 100 degrees Celsius. For example, as the moisture evaporates from product "P", the product may require less heat energy "H" to maintain a given temperature. At the end of the first countdown, algorithm 153 can then start a second countdown of elapsed time that has a given duration, such as ten minutes.
[00090] During the second countdown, algorithm 153 can control the heat output "H" from the radiant heat source 130 according to the temperature measurements received from sensor 160 in order to maintain a uniform decrease in the product temperature from , for example, 100 degrees Celsius for room temperature, whereby the drying operation is complete. Once the product "P" reaches room temperature, or another given temperature, controller 150 can send a signal to operator interface 170 which, in turn, can generate an audible or visual signal detectable by the operator. This audible or visual signal can alert the operator that the drying operation is complete. The operator can then remove the finished, dry product "P" from the apparatus 100.
[00091] Moving now to Figure 3D, a diagram in side elevation is shown of a 100D device which is an alternative configuration according to a fifth modality. The apparatus 100D has an alternative control scheme which can be used in place of the one shown in Figure 3 for the apparatus 100. According to the alternative control scheme which is shown in Figure 3D, the apparatus 100D may comprise a display 177 and a manual heat source control 178. Display 177 is connected to sensor 160 via a communication connection 151. The display is configured to display data relating to at least one product characteristic "P" which is detected and measured by sensor 160.
[00092] Manual heat source control 178 is connected to relay 131 via another communication connection 151. Manual heat source control 178 is configured to receive operator input commands related to the amount of heat "H" produced by the heat source 130. That is, the manual heat source control 178 can be adjusted by the operator to cause the heat source 130 to produce a given amount of heat "H".
[00093] In operation, the operator can initially adjust the manual heat source control 178 to cause the heat source 130 to produce a given amount of "H" heat. The manual heat source control 178 then sends a signal to relay 131 via a communication connection 151. Relay 131 then receives the signal and causes heat source 130 to produce the given amount of heat "H" . The operator then monitors the display 177.
[00094] The sensor 160 can continuously detect and measure a given characteristic of the product "P". The sensor can send a signal to the display 177 which refers to the measured characteristic. The display receives the signal and converts the signal to a value which it displays and which is readable by the operator. The operator can then adjust the heat "H" produced by the heat source 130 in response to information regarding the measured characteristic which is read from the display 177.
[00095] As seen, the apparatus 100, as well as its various other configurations and relative modalities, can allow for a much greater control of the amount of heat that is transferred to the product than can the various apparatus of the prior art.
[00096] Because of this, the apparatus 100 of the present invention can produce "P" products that have a higher quality, and can produce the products in a more efficient manner, than the prior art drying apparatus.
[00097] As is further seen, apparatus 100 may be suitable for a "batch" type of drying processes in which case the support surface 110 is not necessarily moved during the drying operation. In alternative modalities such as those shown in Figures 3A, 3B, and 3C, the support surface 110 can be configured to move the product "P" through the radiant heat source 130 and the sensor 160, in which case a drying process continuous can be achieved. In yet another embodiment of the present invention, which is described below, an apparatus 200 may be specifically suitable for producing a high quality product in a high yield continuous drying process. Drying Appliance with Multiple Control Zones
[00098] Referring to Figure 4, a side elevation view of a drying apparatus 200 according to a sixth embodiment is shown, the apparatus 200 comprises a chassis 210 which can be a rigid structure comprising several structural members including legs 212 and longitudinal structure rails 214 connected thereto. The legs 212 are configured to support the apparatus 200 on a floor 201 or other suitable base.
[00099] Chassis 210 may comprise other structural members, such as transverse reinforcements (not shown) and the like. Chassis 210 can generally be constructed in accordance with known construction methods, including welding, fixing, forming and the like, and can be constructed from known materials such as aluminum, steel and the like. Apparatus 200 is generally elongated and has a first inlet end 216, and a second, opposite, farther end 218.
[000100] The apparatus 200 may further comprise a plurality of substantially parallel transverse rollers 220 which are mounted on the chassis 210 and configured to rotate freely with respect to it. At least one drive roller 222 can also be included in the apparatus 200 and can be supported on the chassis 210 in a substantially transverse mode as shown.
[000101] An actuator 240, such as an electric motor, can be included in the apparatus 200 as well, and can be supported on the chassis 210 next to the drive roller 222. A drive connection 240 can be used to transfer the energy from the actuator 240 for drive roller 222. A speed controller 244, such as an alternating current (AC) variable speed control device or the like, may be included to control the output speed of actuator 240.
[000102] The apparatus 200 comprises a support surface 230, which has a first side 231 and a second opposite side 232. The support surface 230 is supported movable on the chassis 210. The support surface 230 is configured to allow the radiant heat energy passes through it from the second side 212 to the first side 211.
[000103] Preferably, the support surface 230 is made of a material which comprises plastic. Most preferably, the support surface 230 is manufactured from a material selected from the group consisting of acrylic and polyester. Also, preferably the support surface 230 is configured to withstand temperatures of up to at least 148.8 degrees Celsius (300 degrees Fahrenheit). The support surface 230 is configured as a flexible endless belt as shown, at least a portion of which can preferably be substantially flat and level.
[000104] As a form of endless belt, the support surface 230 is preferably supported on the crazy rollers 220 and the drive roller 222. The support surface 230 can be configured to be driven by the drive roller 222 so to be moved, or circular, in the "D" direction with respect to chassis 210. As seen, the support surface 230 can be configured to extend substantially from the input end 216 to the output end 218. A tensioning device 224 it can be supported on the chassis 210 and used to maintain a certain tension on the support surface 230.
[000105] The first side 231 of the support surface 230 is configured to support a product layer "P" on it as shown. The first side 231 is further configured to move product "P" substantially from inlet end 216 to outlet end 218. Product "P" can be in one of many possible forms, including liquid colloidal suspensions, solutions, syrups, and folders. In the case of a liquid "P" product which has a relatively low viscosity, an alternative embodiment of the apparatus which is not shown may include a longitudinal lip, which extends substantially upwards (similar to lip 115 shown in Figure 3) which can be formed on each edge of the support surface 230 to prevent the product from dripping.
[000106] The product "P" can be applied on the first side 213 of the support surface 230 by an application device 252 which may be included in the apparatus 200 and which may be located near the inlet end 216 of the apparatus 200. In the case of a liquid "P" product, the product can be applied to the support surface 230 by spraying, as shown. Although Figure 4 presents a spray method for applying the product "P" to the support surface 230, it is understood that other methods are equally practicable, such as dripping, brushing, and the like.
[000107] Removal device 254 may also be included in apparatus 200. Removal device 254 is located near outlet end 218, and is configured to remove product "P" from support surface 230. Product "P "can be in a dry or semi-dry state when removed from the support surface 230 by the removal device 254.
[000108] The removal device 254 can comprise a sharp curve in the support surface 230 as shown. That is, as shown, the removal device 254 may be configured to cause the support surface 230 to turn sharply around a corner that has a radius which is not greater than approximately twenty times the thickness of the support surface. 230. Also, preferably, the support surface 230 forms a curve in the removal device 254 whose curve is greater than 90 degrees. Most preferably, the curve is approximately between 90 degrees and 175 degrees.
[000109] The type of removal device 254 which is presented may be specifically effective in removing certain types of product "P" which are substantially dry and which exhibit substantially self-adhesive properties. It is understood, however, that other configurations of removal devices 254, which are not shown, can be equally effective in removing various forms of product "P" from the support surface, including scraper blades, low frequency vibrators, and similar. As the product "P" is removed from the support surface 230 at the outlet end 218, a collection hopper 256 can be employed to collect the dry product. Depending on the application, the dry product can be subjected to further processing, such as grinding, crushing or otherwise processing the dry product into a powder.
[000110] The apparatus 200 comprises a heater bank 260 which is supported on the chassis 210. The heater bank 260 comprises one or more first heat sources 261 and one or more second heat sources 262. The heater bank 260 it may also comprise one or more third heat sources 263 and at least one preheater heat source 269. Heat sources 261, 262, 263, 269 are supported on chassis 210 and are configured to direct radiant heat " H "through a gap" G "and towards the second side 232 of the support surface 230.
[000111] Each of the heat sources 261, 262, 263, 269 are dry radiant heat sources as defined above for Figure 3. Heat sources 261, 262, 263, 269 are preferably selected from the group consisting of gas radiant heaters and electric radiant heaters. Furthermore, each of the heat sources 261, 262, 263, 269 is preferably configured to modulate, or to incrementally vary, the amount of radiant heat produced by means of them in a proportional manner. The operation of the heat sources 261, 262, 263, 269 is more fully described below.
[000112] Apparatus 200 may comprise a wrap 246, such as a cover or the like, which is employed to cover the apparatus. Wrap 246 can be configured to contain air conditioning "A" which can be introduced into the wrap via an inlet duct 226. Before entering the wrap, air conditioning "A" can be processed in an air conditioning unit (not shown) in order to have a temperature and humidity which are beneficial for drying the product "P". The air conditioning "A" can circulate through the wrap 246 before leaving the wrap through an outlet duct 228. When leaving the wrap 246, the air conditioning "A" can be returned to the air conditioning unit , or can be ventilated for discharge.
[000113] The apparatus 200 may further comprise a first sensor 281, a second sensor 282, and a third sensor 283. It is understood that, although three sensors 281, 282, 283 are shown, any number of sensors may be included in the apparatus 200. Each of the sensors 281, 282, 283 can be supported on the casing 246, or other suitable structure, in a substantially uniformly spaced mode as shown. Each of the sensors 281, 282, 283 can be any one of a number of sensor types which are known in the art. Preferably, in the case of detecting the temperature of the product "P", each of the sensors 281, 282, 283 is either an infrared sensor or a bimetallic sensor. Preferably, sensors 281, 282, 283 are positioned so as to be substantially exposed to the first side 231 of the support surface 230. Sensors 281, 282, 283 are configured to detect and measure at least one characteristic of the product "P" while the product is supported mobile on the first side 231 of the support surface 230. The characteristics of the product "P" which are detectable and measurable by sensors 281, 282, 283 can include temperature, moisture content, and composition product chemistry. Operational aspects of sensors 281, 282, 283 are more fully described below.
[000114] The apparatus 200 may comprise a controller 250 for controlling various functions of the apparatus during its operation. Controller 250 may include any one of a number of devices such as a processor (not shown), readable memory (not shown), and an algorithm (not shown). Controller 250 will be discussed in further detail below. In addition to controller 250, apparatus 200 may include an operator interface 235 which may be in communication with the controller.
[000115] Operator interface 235 may be configured to transfer information relating to the operation of apparatus 200 to the operator via a display screen 237 such as a CRT or the like. In contrast, operator interface 235 can also be configured to transfer data or operational commands from the operator to controller 250. This can be accomplished by means of a keyboard 239 or similar which can also be in communication with controller 250.
[000116] As seen, a plurality of control zones Z1, Z2, Z3 are defined in the apparatus 200. That is, the apparatus 200 includes at least one first control zone Z1, which is defined in the apparatus between the end of inlet 216 and outlet end 218. A second control zone Z2 is defined in device 200 between the first control zone Z1 and outlet end 218. The device can include additional control zones as well, such as a third zone control zone Z3 which is defined in the device between the second control zone Z2 and the output end. Each control zone Z1, Z2, Z3 is defined to be stationary in relation to chassis 210. A study of Figure 4 will reveal that each first heat source 261 as well as the first sensor 281 are located within the first control zone Z1. Likewise, each second heat source 262 and the second sensor 282 are located within the second control zone Z2. Each third heat source 263, as well as the third sensor 283, are located within the third control zone Z3. It is further evident that the support surface 230 moves the product "P" through each of the control zones Z1, Z2, Z3. That is, as the actuator 240 moves the support surface 230 in the "D" direction, a given portion of the product "P" which is supported on the support surface is moved successively through the first control zone Z1 and then through the second control zone Z2.
[000117] After being moved through the second control zone Z2, the given portion of the product "P" can then be moved through the third control zone Z3 and forward to the removal device 254. As seen, at least a portion of the heater bank 260, like the preheater heat source 269, can be outside any of the control zones Z1, Z2, Z3. Furthermore, a cooling zone 248 can be defined in relation to the chassis 210 and close to the outlet end 218 of the apparatus 200. The cooling zone 248 can be configured to employ any of a number of known means of cooling the product " P "as the product passes through the cooling zone.
[000118] For example, the cooling zone 248 may be configured to employ a cooled heatsink (not shown) such as a cold black body, or the like, which is exposed to the second side 232 of the support surface 230 and the which is positioned inside the cooling zone. Such a heat sink can be configured to cool the product "P" by transferring radiant heat from the product and through the support surface 230 to the heat sink. One type of heatsink which can be so employed can be configured to comprise an evaporator coil which is a portion of a cooling system that uses a fluid refrigerant such as Freon or the like.
[000119] It is understood that the cooling zone 248 may have a relative length which is different from that shown. It is further understood that other means of cooling can be employed. For example, the cooling zone 248 may be configured to incorporate a convection cooling system (not shown) in which the cooled air is directed on the second side 232 of the support surface 230. Furthermore, the cooling zone 248 may be configured to incorporate a conductive cooling system (not shown) in which chilled rolls or the like contact the second side 232 of the support surface 230. The operation of the apparatus 200 may be similar to that of the apparatus 100 according to the first embodiment of the present invention which is described above for Figure 3, except that product "P" is moved continuously passing heat sources 261, 262, 263, 269 and sensors 281, 282, 283. As shown in Figure 4, the product " P "can be applied to the first side 231 of the movable support surface 230 near the inlet end 216.
[000120] The support surface 230 is driven by the actuator 240 through the drive connection 242 and the drive roller 222 in order to rotate in the "D" direction around the crazy rollers 220. The product "P" may be in a substantially liquid state when applied to the support surface 230 by the application device 252. The product "P", which must be dried by the device 200, is fed through it in the feed direction "F" in the direction of the outlet end 218.
[000121] The product "P", while supported on the support surface 230 and moved through the apparatus 200 in the "F" direction, passes through the heater bank 260 which can be positioned in a substantially juxtaposed relationship to the second side 232 of the support surface so as to be exposed to it as shown. The heater bank 260 comprises one or more first heat sources 261 and one or more second heat sources 262 which are configured to direct radiant heat "H" towards the second side 232 and through the support surface 230 for heating the product "P" which is moved in the "F" direction.
[000122] The heater bank 260 may also comprise one or more third heat sources 263 and one or more preheater heat sources 269 which are also configured to direct radiant heat "H" towards the second side 232 to heat the product "P". The product "P", while moving over the support surface 230 in the feed direction "F" is dried by radiant heat "H" to a desired moisture content, and then removed from the support surface at the outlet end 218 by the device of removal 254.
[000123] The product "P" once removed from the support surface 230 can be collected in a collection hopper 256 or similar for storage, packaging, or further processing. The support surface 230, once the product "P" is removed from it, returns to the inlet end 216 whereby an additional product can be applied by the application device 252.
[000124] In order to promote efficient product drying as well as high product quality, air conditioning "A" can be provided by an air conditioning unit (HVAC) 245, and can be circulated around the product " P "by means of wrap 246, inlet duct 226, and outlet duct 228 as the product is moved through the apparatus 200 in the feed direction" F "concurrent with the direction of movement of the product.
[000125] As an additional improvement to the production rate and product quality, a plurality of control zones can be employed. The term "control zone" means a stationary region defined on the apparatus 200 through which the product "P" is moved and in which region the radiant heat is substantially exclusively directed to the product by one or more dedicated heat sources which are regulated independently of heat sources outside the region. That is, a given control zone includes a dedicated servomechanism to control the amount of heat directed to the product "P" which is within a given control zone, where the amount of heat is a function of a measured characteristic of the product.
[000126] As seen, the support surface 230 is configured to move the product "P" in succession through a first control zone Z1 and then through a second control zone Z2. This can be followed by a third control zone Z3. Within the first control zone Z1, one or more first heaters 261 direct radiant heat "H" through gap "G" in the direction of product "P" as the product moves through the first control zone. Likewise, within the second control zone Z2 and within the third control zone Z3, one or more second heat sources 262 and one or more third heat sources 263, respectively, direct radiant heat "H" through the gap "G" in the product direction "P" as the product moves through the second and third control zones, respectively.
[000127] The temperature of, and thus the amount of "H" heat produced by the first radiant heat sources 261 is regulated independently of the temperature of and the amount of heat produced by the second heat sources 262. Similarly, the third heat sources 263 are regulated independently of the first and second heat zones 261, 262. The use of the control zones Z1, Z2, Z3 can provide a greater control of production parameters compared to the devices of the prior art.
[000128] That is, product profiles and specific heat curves can be achieved using the device 200 because the product "P" can be exposed to different amounts of heat "H" in each control zone Z1, Z2, Z3 . Specifically, for example, the first heat sources 261 can be configured to produce heat "H" at a first temperature. Second heat sources 261 can be configured to produce heat "H" at a second temperature which is different from the first temperature. Likewise, third heat sources 263 can be configured to produce heat "H" at a third temperature.
[000129] Thus, as the product "P" continues through the device in the direction of supply "F", the product can be exposed to a different amount of heat "H" in each of the control zones Z1, Z2, Z3. This can be specifically useful, for example, reducing the drying time of the product "P" compared to the drying times of the apparatus of the prior art. This can be achieved by quickly reaching a given temperature of the product "P" and then maintaining the given temperature as the product proceeds in succession through the control zones Z1, Z2, Z3. The use of the control zones Z1, Z2, Z3 can also be useful in providing a close control of the amount of heat "H" which is transmitted to the product "P" in order to provide a higher product quality. That is, the product quality can be improved using the control zones Z1, Z2, Z3 to minimize the overexposure and underexposure of the product "P" to the heat energy "H".
[000130] Assuming that a given product "P" is relatively moist and at room temperature when placed on the support surface 230 by the application device 262, a relatively large amount of heat "H" is required to increase the temperature of the product to a given temperature such as 100 degrees Celsius. Thus, a preheater heat source 269 can be employed to preheat product "P" before the product enters the first control zone Z1. The preheater heat source 269 can be configured to continuously produce radiant heat "H" at a maximum temperature and direct a maximum amount of heat "H" to the product "P".
[000131] As the product "P" enters the first control zone Z1, the first heat sources 261 within the first control zone Z1 can be configured to produce an amount of heat "H" which is sufficient to achieve the given desired product temperature. The first sensor 281 together with the controller 250, can be used to regulate the temperature of the first heat sources 261 in order to transfer the desired amount of heat "H" to the product "P". The first sensor 281 is configured to detect and measure at least a given characteristic of the product "P" while the product is within the first control zone Z1. For example, the first sensor 281 can be configured to detect and measure the temperature of the product "P" while the product is within the first control zone Z1.
[000132] The first sensor 281 can detect and measure a characteristic of the product "P" while the product is within the first control zone Z1 and then transfer this measured characteristic to the controller 250. The controller 250 can then use the measurement of the first sensor 281 to modulate the temperature, or heat emission, of the first heat sources 261. That is, the heat "H" produced by the first heat sources 261 can be regulated as a function of a measured product characteristic of the product " P "within the first control zone Z1 as detected and measured by the first sensor 281. This measured product characteristic can include, for example, the product temperature.
[000133] The second sensor 282 is similarly used to detect and measure at least one characteristic of the product "P" while the product is within the second control zone Z2. Likewise, the third sensor 283 can be used to detect and measure at least one characteristic of the product "P" while the product is within the third control zone Z3.
[000134] The product characteristics detected and measured by the second and by the sensors 282, 283 within the second and third control zones Z2, Z3, respectively, can be similarly used to modulate the amount of heat "H" produced by second and third heat sources 262, 263 to maintain a specific temperature profile of the product "P" as the product progresses through each of the control zones.
[000135] In the event that the product "P" is heated quickly to a given temperature and then maintained at the given temperature, the first heat sources 261 are likely to produce heat "H" at a relatively high temperature in order to rapidly increase the product temperature for the given temperature by the time the product "P" leaves the first zone Z1. Assuming that the product "P" is at a given temperature when entering the second control zone Z2 the second and third heat sources 262, 263 will produce heat "H" at successively lower temperatures because less heat "H" is required for maintain the temperature of the product as its moisture content decreases.
[000136] As mentioned above, sensors 281, 282, 283 can be configured to detect and measure any of a number of product characteristics such as moisture content. This can be specifically beneficial for the production of a high quality "P" product. For example, in the above case where the product temperature has reached the given temperature as the product "P" enters the second control zone Z2, the second and third sensors 282, 283 can detect and measure the moisture content of the product as the product progresses through the respective second and third control zones Z2, Z3.
[000137] If the second sensor 282 detects and measures a relatively high product moisture content of the product "P" within the second control zone Z2, then controller 250 can modulate the second heat sources 262 in order to continue to maintain the product temperature at the given temperature in order to continue to dry the product. However, if the second sensor 282 detects a relatively low product moisture content, then the controller 250 can modulate the second heat sources 262 in order to reduce the product temperature in order to prevent the product "P" from drying out.
[000138] Likewise, the third sensor 283 can detect and measure the moisture content of the product within the third control zone Z3, whereby the controller can determine the appropriate amount of heat "H" to be produced by the third parties heat sources 263. Although three control zones Z1, Z2, Z3 are presented, it is understood that any number of control zones can be incorporated according to the present invention.
[000139] In support of the description of the interaction between controller 250, sensors 281, 282, 283, and heat sources 261, 262, 263 provided by the example above, a given control zone Z1, Z2, Z3 can be described as a separate, independent, and exclusive control loop which comprises each associated sensor and each associated heat source located within the given control zone, and which, together with the controller, is configured to independently regulate the amount of heat " H "produced by the associated heat sources as a function of at least one characteristic of the product" P "measured by the associated sensor.
[000140] That is, each sensor 281, 282, 283 associated with a given control zone Z1, Z2, Z3, can be considered as configured to provide a control return to the controller 250 exclusively with respect to the characteristic of a portion of the product "P" which is within the given control zone. Controller 250 may use the feedback to adjust the output of heat sources 261, 262, 263 according to a temperature profile or other such parameters defined by the operator or otherwise stored in the controller.
[000141] In addition to decreasing the drying time of the product "P" compared to the drying apparatus of the prior art, the plurality of control zones Z1, Z2, Z3 of the apparatus 200 can also be used to achieve specific product profiles which can be beneficial for the quality of the product as described above for the apparatus 100.
[000142] For example, it can be assumed that the quality of a given product "P" can be maximized by following a given product temperature profile during drying. The given product temperature profile can dictate that, as the product "P" passes successively through the first, second, and third control zones Z1, Z2, Z3, the temperature of the product initially increases rapidly to a given maximum temperature, the from where the temperature of the product "P" gradually decreases until it is removed from the support surface 230.
[000143] In this case, the first sensor 281, the first heat sources 261 and the controller 250 can operate in a similar way to that described above in order to quickly increase the temperature of the product "P" to a first temperature which can be reached as the product "P" passes through the first control zone Z1. The first temperature can correspond to a relatively large amount of heat "H" which is transferred to the product "P" which initially contains a high percentage of moisture.
[000144] As the product "P" passes through the second control zone Z2, the second sensor 282, the second heat sources 262 and the controller 250 can operate to lower the product temperature to a second relatively average temperature which is lower than the first temperature. The second temperature may correspond to a lower amount of heat "H" which is required since the moisture content of the product "P" drops.
[000145] Likewise, as the product "P" passes through the third control zone Z3, the third sensor 283, the third heat sources 263 and the controller 250 can operate to further lower the product temperature to a third temperature relatively low which is lower than the second temperature. The third temperature can correspond to a relatively low amount of heat "H" which is required as the product "P" approaches the desired dryness.
[000146] In addition to regulating the temperature of the heat sources 261, 262, 263, the controller 250 can also be configured to regulate the speed of the support surface 230 in relation to the chassis 210. This can be achieved by configuring the controller 250 so to modulate the speed of actuator 240. For example, as in the case where actuator 240 is an AC electric motor, the controller may be configured to modulate the variable speed control unit 244 by means of a servo or similar.
[000147] The speed, or rate of movement, of the support surface 230 can affect the drying process of the product "P" which is performed by the apparatus 200. For example, a relatively low speed of the support surface 230 can increase the amount of heat "H" which is absorbed by product "P" because the lower speed will cause the product to be exposed to heat "H" for a longer period of time. In contrast, a relatively fast speed of the support surface 230 can decrease the amount of heat "H" which is absorbed by the product "P" because the faster speed will result in a shorter exposure time during which the product is exposed to the heat.
[000148] Furthermore, controller 250 can also be configured to regulate various qualities of air conditioning "A" which can be circulated through wrap 260. For example, controller 250 can be made to regulate the flow rate, the relative humidity, and the air conditioning temperature "A". These qualities of the "A" air conditioner can have an effect on both the drying time and the quality of the "P" product.
[000149] In another alternative embodiment of the apparatus 200 which is not shown, the casing 246 may be configured so as to be substantially sealed against external atmospheric air. In this case, the chemical composition of the air conditioner "A" can be controlled to affect the drying process in specific ways, or to affect or preserve the chemical properties of the product "P". For example, air conditioning "A" can substantially be an inert gas which can act to prevent oxidation of product "P".
[000150] Moving to Figure 5, a schematic diagram is shown which presents a possible configuration of the device 200 which comprises a plurality of communication connections 257. The communication connections 257 are configured to provide the transmission of data signals between the various components of the apparatus 200. Communication connections 257 can be configured as any one of a number of possible means of communication, including those of wiring and fiber optics. In addition, communication connections 257 may comprise a wireless communication medium that includes infrared wave, microwave, sound wave, radio wave and the like.
[000151] A readable memory storage device 255, such as a digital memory, can be included in the controller 250. The readable memory device 255 can be used to store data relating to the operational aspects of the device 200 which are received by the controller via communication connections 257, as well as setpoints and other stored values and data which can be used by controller 250 to control the drying process. Controller 250 may also include at least one algorithm 253 which can be employed to perform various decision-making processes required during the operation of apparatus 200.
[000152] The decision-making processes taken into account by the 253 algorithm may include maintaining an integrated coordination of the various variable control aspects of the device 200. These variable control aspects comprise the speed of the support surface 230, the amount of heat " H "produced by each of the heat sources 261, 262, 263, 269, and product characteristic measurements received from sensors 281, 282, 283. In addition, the 253 algorithm may be required to perform the decision-making processes operating according to various adjusted production parameters such as a product temperature profile and a production rate.
[000153] Communication connections 257 can provide data transmission between controller 250 and operator interface 235 which may comprise a display screen 237 and a keyboard 239. That is, communication connections 257 between controller 250 and operator interface 235 can provide data communication from the controller to the operator via the display screen. Such data may include various aspects of the apparatus 200 including the temperature and moisture content of the product "P" with respect to the position of the product within each of the control zones Z1, Z2, Z3.
[000154] In addition, such data may include the speed of the support surface with respect to chassis 210 and the temperature of each of the heat sources 261, 262, 263, 269. Communication connections 257 can also provide that data is operator communications to controller 250 via keypad 239 or similar. Such data may include operational commands that include the specification by the operator of a given product temperature profile.
[000155] A communication connection 257 can be provided between the controller 250 and the HVAC unit 245 in order to communicate the data between them. Such data may include controller commands 250 for HVAC unit 245 which specify a given temperature, humidity, or similar, for air conditioning "A". A communication connection 257 can also be provided between controller 250 and actuator 240 in order to communicate data between them. These data can include commands from the controller 250 to the actuator which specify a given speed of the support surface 230.
[000156] Additional communication connections 257 can be provided between controller 250 and each of sensors 281, 282, 283 in order to communicate data between each of the sensors and the controller. Such data may include measurements of various characteristics of the product "P" as described above for Figure 4. Other communication connections 257 can be provided between controller 250 and each of the heat sources 261, 262, 263, 269 in order to provide data transmission between them.
[000157] This data can include controller commands 250 for each of the heat sources 261, 262, 263, 269 which instruct each of the heat sources as to the amount of heat "H" to produce. As can be seen, apparatus 200 may include a plurality of control devices 233, which may comprise electrical relays, in which each of the control devices is connected via communication connections 257 on controller 250. Each of the devices control unit can be configured in control device mode 131 which is described above for Figure 3.
[000158] According to a seventh embodiment of the present invention, a method of drying a product includes providing a support surface which has a first side, and a second opposite side, and which supports the product on the first side while directing radiant heat towards the product. Preferably, the support surface can allow radiant heat to pass through it in order to heat the product. The support surface can be a substantially flexible sheet. Alternatively, the support surface can be substantially rigid.
[000159] The method can also include the step of measuring a product characteristic, together with the regulation of the amount of radiant heat directed to the second side as a function of the measured characteristic. The measured characteristic may include the temperature of the product, the moisture content of the product, and the chemical composition of the product. The characteristic can be detected and measured intermittently at given intervals, or it can be measured continuously over a given time interval.
[000160] The method may also include moving the support surface in order to move the product through the heat source. Alternatively, the method may include moving the support surface in order to move the product through a plurality of control zones in succession and providing a plurality of heat sources, where each control zone has at least one heat source associated with it. dedicated exclusively to direct radiant heat within the associated control zone.
[000161] In other words, the method may include regulating the temperature of the heat sources within any given control zone regardless of the temperature of any other heat sources outside the given control zone. This can make it possible to produce and maintain a given product temperature profile as the product is moved through the control zones.
[000162] The method may also include providing a plurality of sensors, in which any given control zone has at least one sensor dedicated exclusively to the detection and measurement of at least one characteristic of the product within the given control zone. This can make it possible to regulate the temperature of each heat source in any given control zone as a function of at least one characteristic of the product within the given control zone. As noted above, characteristics can include temperature, moisture content, and the chemical composition of the product, among others.
[000163] The rate of movement of the support surface to the control zones can also be regulated according to the method. In addition, a wrap can be provided to assist in the circulation of air conditioning around the product as the product is processed by the appliance. The quality of the air conditioner can be controlled, where such qualities can include the temperature, humidity, and the chemical composition of the air conditioner. The method may include annealing the product whose product is supported on the support surface. Drying Appliance with Mobile Heaters
[000164] Another aspect of the present invention relates to a drying apparatus that is capable of independently controlling the temperature of the product being heated (for example, to achieve a desired temperature profile) and the radiation wavelength ( for example, to maximize the heat transfer rate). For such purposes, a drying apparatus may be provided with one or more heat sources that are mobile in relation to the product "P" in order to increase or decrease the gap or spacing between the heat source and the product "P". By adjusting the gap between the product and the heat source, it is possible to control the source temperature in such a way that it produces the desired product temperature and radiation wavelength. For example, as noted above, if a specific drying profile requires that the product temperature remains substantially constant across one or more control zones, then the product is typically subject to less heat in each successive control zone. To maintain the desired product temperature and radiation wavelength, heaters in a control zone can be moved further away from the product to decrease the heat applied to the product while maintaining the source temperature to produce radiation at the desired wavelength. . For example, if desired, the source temperature and heater positions can be controlled to produce a predetermined constant wavelength in successive zones to compensate for changes in energy required to evaporate moisture as the moisture content in the product decreases as it does. it is dried through each of the zones.
[000165] Alternatively, if desired, the source temperature can be adjusted to produce a desired wavelength in a control zone that is different than the wavelength in the preceding control zone and the gap between the heat source and the product can be adjusted accordingly to reach the desired product temperature. This allows the dryer to compensate for other product characteristics that may vary within each zone or zone from zone to zone during the drying process, such as product emissivity, product thickness, changes in product sensitivity (or specific compounds in the product) for a specific wavelength of IR (infrared radiation), and the ability to release restricted moisture within the product (the ability to release restricted moisture decreases as the product is dried). The controller and dryer can be configured to continuously monitor the wavelength of the heat sources and the temperature of the product during the drying process, and automatically adjust the temperature and positions of the heat sources to maintain the temperature of the product and the desired wavelength within each heating zone.
[000166] Referring now to Figure 6, a drying apparatus 200A is shown, according to an eighth embodiment of the present description. The drying apparatus 200A is a modification of the drying apparatus 200 of Figures 4 and 5. A difference between the drying apparatus 200A and the drying apparatus 200 is that the drying apparatus 200A has heat sources which are upward and downward movable in relation to the product "P". The drying apparatus 200A includes a chassis 300 which is modified in relation to chassis 210 of Figure 4 by the fact that it includes movable platforms, or heater supports 302, 304, 306, 308 that support the heat sources 269, 261, 262, 263, respectively. The heat sources 269, 261, 262, 263 can comprise heating elements that produce radiant heat in the infrared spectrum. Each platform 302, 304, 306, 308 is mounted on a pair of vertical legs 310 of the chassis 300 and is configured to move up or down relative to it, as indicated by the double-headed arrows 312.
[000167] In a specific embodiment, each heater support supports a set of one or more quartz heating elements to produce infrared radiation. Each such heating element may comprise a coiled wire contained in a quartz pipe. The quartz tubing can be matte, as is known in the art, to increase the heat capacitance of the heating element. The quartz tubing can include additives, such as silicon or graphite, to further increase the heat capacitance in the heating element. The increased heat capacitance can provide better control of the operating temperature of the heating element, such as if a switch or relay of the "on / off" type was used to modulate the current for the heating elements.
[000168] As shown in Figure 6, each heat source within a Z1, Z2, or Z3 control zone is supported on a common platform, and therefore each heat source within a specific control zone moves up and down. low joins. In alternative modes, less than three heat sources can be mounted on a single platform. For example, each heat source can be mounted on a separate platform and its vertical position can be adjusted in relation to other heat zones within the same control zone. In still other embodiments, a single platform can extend into multiple zones to support heat sources in adjacent control zones.
[000169] Mounted within each heating zone (control zones Z1, Z2, Z3 and preheating zone PH) directly above a heat source are one or more temperature detection devices for the heat sources, such as one or more thermocouples 314. Each thermocouple 314 is positioned to monitor the surface temperature of the heating elements of a corresponding heat source and is in communication with the controller 250 (Figure 5). As described in more detail below, a return control loop is provided to continuously monitor the temperature of the heat sources within each heating zone and adjust the vertical position of the heat sources and / or the temperature of the heat sources to achieve a predetermined wavelength and a predetermined product temperature using radiant energy. In the illustrated mode, a thermocouple is located within each heating zone. However, in other embodiments, more than one thermocouple can be used within each heating zone. For example, if each heat source is mounted on its own platform, then it would be desirable to place at least one thermocouple above each heat source. A thermocouple 314 can be mounted in any convenient position adjacent to the heating elements of a corresponding heat source. For example, the thermocouple can be mounted on the support structure or container of a heat source that supports one or more heating elements.
[000170] In place of or in addition to thermocouples, the dryer may include in each heating zone one or more sensors, such as an infrared spectrometer or radiometer, to measure the energy or the wavelength of infrared energy that reaches the product . Such sensors can be mounted at any convenient locations in the dryer, such as directly above the support surface 230 and the product, preferably directly above an edge region of the support surface that is not covered by the product layer. This method has the advantage of allowing the system to compensate for changes in the actual IR wavelength that reaches the product which may vary due to the transparency and refractive properties of the support surface 230, as well as the IR energy that is emitted from the surfaces heater container or reflectors in the heater containers. Wavelength or energy sensors can replace heater thermocouples 314 (or can be used in combination with thermocouples) as a means of determining the wavelength of radiant energy emitted from heat sources in a control scheme by whereby the vertical positions of the heat sources and / or their temperatures are adjusted to achieve a predetermined wavelength and a predetermined product temperature within each zone.
[000171] Any suitable techniques or mechanisms can be used to carry out the vertical movement of each platform 302, 304, 306, 308 in relation to the support legs 310. Figure 7, for example, is a schematic illustration of the Z1 control zone showing platform 304 having drive gears 316 mounted on opposite sides of the platform. Each drive gear 316 engages a respective rack gear 318 mounted on a respective support leg 310 of the chassis. The drive gears 316 can be powered by an electric motor 320 mounted in a convenient location on the platform. The motor 320 can be operatively coupled to each drive gear 316 by a drive shaft (not shown) so that the operation of the motor is effective for driving the drive gears, which translate along the rack gears to move the gear. platform up or down. Motor 320 is in communication with controller 250 (Figure 5), which controls the vertical position of the platform. The platforms in the other heating zones may have a similar configuration.
[000172] Figure 9 shows an alternative configuration to effect the vertical movement of a platform. In this modality, a platform 304 is mounted on four linear actuators 350 (one mounted on each corner of the platform), although a greater or lesser number of actuators can be used. Each actuator 350 in the illustrated embodiment comprises a threaded shaft 352 and a nut 354 disposed on the shaft. The platform 304 is supported on the upper ends of the axles 342. A synchronized rotation of the nuts 354 (controlled by the controller 350) causes the platform 304 to be raised or lowered in relation to the conveyor 230. It should be noted that several other mechanisms can be used to carry out the vertical movement of the platforms. For example, any of several pneumatic, electromechanical, and / or hydraulic mechanisms can be used to move the platform up and down, including various types of linear actuators, screw motors, screw rails, and the like.
[000173] As can be appreciated, adjusting the vertical position of the heat source (s) on a platform adjusts the clearance or G spacing between the heat source (s) and the supported "P" product on the support surface 230. The temperature of the product varies according to the distance between the heat source and the product, as well as the temperature of the heat source. Increasing the distance from the heat source to the product will decrease the temperature of the product while decreasing the distance from the heat source to the product will increase the temperature of the product (if the temperature of the heat source remains constant). As noted above, the wavelength of radiant energy emitted from a heat source can be increased and decreased by decreasing and increasing, respectively, the temperature of the heat source. Consequently, the temperature of the product "P" within the heating zone and the wavelength of radiant energy absorbed by the product within this heating zone can be independently controlled by adjusting the temperature of the heat source (s) and the distance between the heat source (s) and the product.
[000174] In specific modalities, controller 250 can be configured to continuously monitor the temperature of the product (and / or other characteristics of the product) through sensors 281, 282, 283 and the temperature of the heat sources through thermocouples 314 and adjust automatically the vertical position of the heat sources to maintain a predetermined temperature profile for the product and a predetermined wavelength of radiant energy in each heating zone. In order to determine the wavelengths of radiant energy from the heat sources, the controller 250 may include an algorithm or a look-up table that is used by the controller to determine the wavelength that corresponds to each heat source based on the readings temperature values of thermocouples 314 that are transferred to the controller.
[000175] In an implementation, the wavelength of a heat source can be determined by measuring the temperature of the heat source and calculating the wavelength using Wien's law (Àmax = b / T, where Àmax is the length of peak wave, b is the Wien displacement constant and T is the temperature of the heat source). In another implementation, the wavelength of a heat source can be determined by measuring the temperature of the heat source and identifying the corresponding peak wavelength of the heat source in a graph, as shown in Figure 10. Alternatively, the The dryer can include wavelength sensors (as discussed above) that directly monitor the wavelengths of radiant energy from each heat source and transfer the signals to the controller.
[000176] Controller 250 may be in communication with a plurality of control devices 233 (Figure 5) that control the temperatures of the heating elements in each zone. Desirably, a control device 233 is provided for each zone of the dryer. For example, control devices 233 can be solid-state relays that modulate the electrical current to the heating elements using an "on / off" control scheme. Most desirably, control devices 233 comprise phase angle control modules that can increase or decrease the temperature of the heating elements by varying the voltage for the heating elements. Each phase angle control module 233 is in communication with the controller 250 and, based on signals received from the controller, varies the input voltage for the heating elements of a respective zone in order to increase or decrease the operating temperature heating elements. The use of the 233 phase angle control modules is advantageous in that it allows precise control over the operating temperatures of the heating elements in order to better achieve the desired product temperature profile.
[000177] The wavelength of infrared waves emitted from the heat sources in each zone can be selected based on the desired heating and drying characteristics for a specific product at a specific drying stage as well as various product characteristics, such as emissivity and the ability to absorb radiant heat. For example, the wavelength in each heating zone can be selected to maximize the rate of absorption of radiant energy in each heating zone for a specific product. Figure 11 shows the absorption of electromagnetic radiation by water. In the infrared range, there is a peak at approximately 3 μm and approximately 6.2 μm. In a specific implementation, it may be desirable to maintain a constant wavelength across the entire drying process at approximately 3 or 6.2 μm for optimal absorption of IR energy by the water in the product being evaporated. As the moisture content of the product applied to the support surface 230 varies as does the moisture in the product as it moves through each heating zone (as well as other product characteristics), the amount of heat required to achieve a desired product temperature in each zone can vary substantially. Consequently, the positions of the heat sources can be automatically adjusted to maintain a predetermined constant wavelength and a predetermined temperature profile. Moving the heaters produces a constant wavelength to compensate for changes in the moisture content of the product during drying, and to compensate for different desired product temperature setpoints in each drying zone (that is, the temperature profile of desired drying time, which may vary for different products). In some cases it may be desirable to operate some heat sources at 3 μm in some drying zones (such as in the initial zones where relatively higher temperatures are needed) and at 6.2 μm in other drying zones (such as in the zones in the direction of the end of the dryer where relatively lower temperatures are needed). In this way, the specific wavelength (3 or 6.2 μm) for each zone can be selected based on whether the zone has any specific limitations or temperature requirements.
[000178] In other implementations, it may be desirable to change the wavelength in each successive zone for one or more reasons. For example, the emissivity of the product as a whole may change as it proceeds through the drying process. As such, the wavelength in each heating zone can be selected to maximize the absorption of radiant energy by the product as the emissivity of the product changes during the drying process. As another example, the wavelength in each heating zone can be selected to achieve a desired degree of penetration of radiant waves into the product or to compensate for changes in the thickness of the product layer as it dries. Furthermore, the sensitivity of the product (or a specific compound in the product) to a specific IR wavelength may increase as the product moves through the dryer. Thus, the wavelength in each heating zone can be selected to avoid damage to the product or specific compounds in the product.
[000179] The following describes a specific proposal for operating the 200A dryer to dry a product using a predetermined IR wavelength. As noted above, infrared wavelengths of approximately 3 microns and 6.2 microns generally produce the best rate of absorption of radiant energy into water. Thus, controller 250 can be programmed to control the temperature of the heat sources in each heating zone to produce infrared waves of, for example, 3 microns (or alternatively 6.2 microns) across all heating zones. To maintain a predetermined temperature profile for the product, controller 250 monitors the temperature of the product and continuously adjusts the spacing between the heat sources and the product as needed to maintain the desired temperature of the product within each zone. As discussed above, to dry certain products it is desirable to maintain a constant product temperature across zones Z1, Z2, Z3. As the moisture content of the product decreases as the product moves through each zone, less heat is needed in each successive zone to maintain the desired product temperature. As such, the heat sources in the first control zone Z1 are typically closer to the product than the heat sources in the second control zone Z2, which are typically closer to the product than the heat sources in the third control zone. Z3, as shown in Figure 6. As can be seen, heat sources can operate at constant or substantially constant operating temperatures, and the controller can cause the positions of the heat sources to move up or down to vary the amount of heat reaching the product. An advantage of operating heat sources at constant, or substantially constant operating temperatures is that the heat sources can be operated on a constant or substantially constant power supply and voltage, which can significantly increase the energy efficiency of the dryer.
[000180] An alternative control scheme for operating the 200A drying apparatus is illustrated in the flow chart illustrated in Figure 8 and can operate in the following way. When the dryer is initially turned on and the product is first applied to the support surface 230, the heat sources are in a starting position (usually, but not necessarily, all heat sources are in the same vertical position). Referring to Figure 8, the controller first reads the product temperature (402) and adjusts the operating temperatures of the heat sources accordingly to achieve the desired product temperature in each heating zone (404 and 406). If the product temperature is at the predetermined set point for the product in a specific zone, then the controller reads the operating temperature of the heat sources and determines the wavelength produced by the heat sources in that zone (408 and 410). Alternatively, the wavelength in the heating zone can be determined from signals transferred to the controller from a spectrometer, radiometer, or equivalent device.
[000181] If the wavelength in a specific zone is greater or less than a predetermined wavelength, the controller controls the heat sources in that zone to move further or closer to the product (412 and 414). More specifically, if the measured wavelength is greater than the predetermined wavelength, then the controller causes the heat sources to move further away from the product, and if the measured wavelength is less than the wavelength. predetermined wave, then the controller causes the heat sources to move closer to the product. As the heat sources move further or closer to the product, the temperature of the product may begin to decrease or increase, respectively. Consequently, the process loop resumes at block 402 where the controller reads the product temperature and increases or decreases the operating temperature of the heat sources until the predetermined product temperature is again achieved. At this point, the controller again determines the wavelength produced by the heat sources (408 and 410) and causes the heat sources to move further or closer to the product if the wavelength is even greater or less than than the predetermined wavelength for this zone (412 and 414). This process loop is repeated until the heat sources produce energy at the predetermined wavelength. At this point, the controller again determines the product temperature (402 and 404), adjusts the operating temperature of the heat sources as necessary to maintain the predetermined product temperature (406) and then compares the measured wavelength with the length of predetermined wave (410 and 412) and moves heat sources if the measured wavelength is greater or less than the predetermined wavelength (414).
[000182] When the controller determines that the heat sources in a zone must be moved (either up or down), the heat sources can be moved in small, predetermined increments of block 414 after each incremental movement, the controller reads the product temperature (402), increases or decreases the operating temperature of the heat sources to achieve the predetermined product temperature (406), and once the predetermined product temperature is achieved (404), the controller determines the length of wave produced by the heat sources (408 and 410), and then causes the heat sources to move another increment if the wavelength is longer or shorter than the predetermined wavelength (414).
[000183] The way of operating the dryer illustrated in Figure 8 can improve the responsiveness of the dryer (that is, the capacity of the system to increase or decrease the amount of heat applied to the product as needed to avoid overheating or underheating the product) compared to a control scheme where the heating elements are kept at a constant temperature and are raised or lowered to adjust the amount of heat applied to the product. The method shown in Figure 8, therefore, includes two return loops, namely, a first return loop that adjusts the temperature of the heating elements in response to sudden changes that require an immediate increase or decrease in the amount of heat applied to the product, and a second feedback loop that adjusts the positions of the heating elements until the target wavelength is achieved at the optimum product temperature. A variety of process characteristics vary during the drying process and can cause a demand for a sudden increase or decrease in the amount of heat that must be applied to the product in order to maintain the product's targeted temperature profile. Some of these characteristics include the moisture and solids content of the product applied to the carrier, the initial product temperature, the rate and thickness of product applied to the carrier, and the ambient conditions (temperature and relative humidity). Operating two return loops in the described mode allows the operating temperatures of the heating elements to be increased or decreased quickly in order to respond to a demand for an increase or decrease in the amount of heat applied to the product in order to avoid overheating or overheating of product.
[000184] In another implementation, controller 250 can be programmed to increase and decrease the temperature of a heat source within a predetermined temperature range that corresponds to an acceptable wavelength spectrum before adjusting the position of the heat source . For example, controller 250 can monitor the product temperature and adjust the temperature of a heat source within a predetermined range as necessary to maintain the temperature profile. If the temperature of the heat source exceeds or falls below the predetermined range, the controller can then move the heat source closer to or further from the product as needed to maintain the temperature profile for the product. This way of operating the dryer allows very rapid responses from heat sources to changes in the amount of heat required to achieve the desired product temperature in each drying zone. Further explaining, a target temperature is selected for each heater to achieve a desired wavelength, but in order to respond quickly, the heater temperature is varied within a specified and limited range within an acceptable wavelength band. This allows heat sources to respond quickly to small changes, in real time, in the product being dried, such as changes in moisture content or product thickness that can occur frequently, thereby avoiding overheating or underheating the product.
[000185] In the illustrated mode, controller 250 operates in a first return loop to control the temperature of the heat sources and in a second return loop to control the spacing of the heat sources in relation to the product. In alternative modes, the temperature of the heat sources and their positions in relation to the product can be manually adjusted by an operator. For example, the operator can monitor the various operating parameters of the process (product temperature, heat source temperature, etc.) and make adjustments to one or more of the operating parameters by entering the information on the 269 keypad, whose information is transferred for controller 250.
[000186] The drying apparatus 200A in the illustrated embodiment is described in the context of drying a thin layer of liquid product. It should be understood that all of the drying apparatus modalities described herein can be used to dry or otherwise apply heat to non-fluid food products (eg baked goods, rice) or any of several non-food products (eg wood products, sludge, film plate, textiles, adhesives, paints, photosensitive layers, etc.). EXAMPLE 1: Dehydrating Beet Juice Concentrate
[000187] Example 1 demonstrates the improved capacity that can be achieved by adjusting the position of the heaters in relation to the product conveyor and the outlet of the heaters. In this example, a drying device that has 16 zones was used to dehydrate a beet juice concentrate in a first drying run and a second drying run. The dehydrated beet juice concentrate was processed into a powder. Tables 1 and 2 show the dryer zone settings in the first and second runs, respectively. The heater distance in Tables 1 and 2 represents the distance between the heating elements and the conveyor in each zone. Table 3 shows other dryer operating parameters and product characteristics for the first and second runs. The product set points across all zones (which determines the product's temperature profile) were the same for each run. However, in the first drying run, the position of the heaters was manually adjusted before the dryer operation in order to cause the dryers to emit an infrared radiation at or around 6.2 μm (corresponding to the "C" peak in the Figure 11). In the second drying run, the position of the heaters was manually adjusted before the dryer operation in order to cause the dryers to emit infrared radiation at or around 7.0 μm (corresponding to the "D" peak in Figure 11) . The wavelength of infrared radiation in each zone was determined by measuring the temperature of the heating elements and calculating the wavelength using Wien's law.
[000188] Figure 12 shows the temperature of the heating elements in each zone of the dryer during the first drying run. Figure 13 shows the temperature of the heating elements in each zone of the dryer during the second drying run. Figure 14 shows the graphs of Figures 12 and 13 on a graph. Figure 15 shows the wavelength of IR radiation measured in each zone for the first and second drying runs.
[000189] Example 1 demonstrates that even with the manual positioning of the heaters, the product temperature and the wavelength of the heaters can be independently controlled. A much higher degree of precision in controlling the wavelength of infrared radiation across all zones can be achieved by a continuous and automatic temperature adjustment of the heating elements and the position of the heating elements in relation to the conveyor. Table 4 compares the yield (drying capacity) and the energy use of the two drying runs. It can be seen from the results in Table 4 that targeting 6.2 μm across all zones (drying run 1) resulted in a 53% increase in drying capacity compared to targeting 7.0 μm across all zones ( drying run 2). In addition, drying run 1 used less energy per kilogram of dry product than in drying run 2, most likely because the energy was more efficiently absorbed by the water in the product (which causes the product to release moisture).
[000190] Most importantly, Example 1 shows that extremely high product quality can be achieved (as evidenced by the moisture content in both drying runs) by drying the product at the predetermined temperature profile while the drying capacity of the dryer can be increased substantially by operating the heating elements at a predetermined wavelength. In other words, the capacity of the dryer can be significantly improved by operating the heating elements at a predetermined infrared wavelength that maximizes the absorption of infrared radiation in the product, while also maintaining a high product quality by precisely controlling the product temperature accordingly. it's dry. When dehydrating liquid food products, such as fruit or vegetable liquids, it is important to produce a high quality product that is low in moisture content (for flowability and shelf life) with minimal nutritional loss.


Table 4: Summary of Results for Beet Juice Concentrate EXAMPLE 2: Dehydrating Fruit Puree Mix
[000191] In Example 2, a 16-zone dryer was used to dry a fruit puree mixture comprising a mixture of grape puree and blueberry puree. The fruit puree mixture was dried in four separate drying runs all having the same product temperature set points. The dehydrated fruit puree mixture was processed into a powder. The first drying run (zone adjustments shown in Table 5) represents the "baseline" operating conditions where the heating elements across all zones are set at the same distance from the conveyor. In the second drying run (zone adjustments shown in Table 6), the position of the heaters was kept the same as in the drying run 1 but the product rate applied on the conveyor was increased to increase the dryer capacity. In the third drying run (zone adjustments shown in Table 7), the position of the heaters was manually adjusted before the dryer operation in order to cause the heaters to emit an infrared radiation at or around 6.2 μm (corresponding to to peak "C" in Figure 11). In the fourth drying run (zone adjustments shown in Table 8), the position of the heaters was manually adjusted before the dryer operation in order to cause the heaters to emit infrared radiation at or around 7.0 μm (corresponding to to the "D" peak in Figure 11). The wavelength of infrared radiation in each zone was determined by measuring the temperature of the heating elements and calculating the wavelength using Wien's law. Table 9 summarizes other operating parameters and product characteristics for all four drying runs.
[000192] Figures 16, 17, 18, and 19 show the temperature of the heating elements in all areas of the dryer for the first, second, third, and fourth drying runs, respectively. Figure 20 shows the line graphs in Figures 16-19 on a graph. Figure 21 shows the wavelength of IR radiation measured in each zone for all four drying runs.
[000193] Table 10 compares the yield (drying capacity) and energy use of all four drying runs. It can be seen from the results in Table 10 that targeting 6.2 μm across all zones (drying run 3) resulted in a 55% increase in drying capacity compared to the second drying run where the position of the heaters was not adjusted. Drying run 3 also provided the lowest energy consumption per kilogram of dry product.
[000194] Like Example 1, Example 2 shows that extremely high product quality can be achieved (as evidenced by the moisture content in all drying runs) by drying the product at the predetermined temperature profile while the drying capacity of the dryer can be increased substantially by operating the heating elements at a predetermined wavelength.



Table 10: Summary of Results for Mixing Fruit Puree
[000195] The following factors can affect the dryer's ability to control the wavelength and product temperature within a control zone: (i) the adjustment range of the heating elements towards and away from the belt support surface shipping company; (ii) the watts density of the heating elements; (iii) the spacing between the heating elements; and (iv) the reflector configuration of the heating elements. These features can be optimized within each control zone to maximize dryer capacity and product quality.
[000196] If a heating element is too close to the conveyor (for example, closer than the spacing between the individual heating elements), hot / cold areas on the conveyor belt can result if the infrared beam rays from heating elements adjacent heating elements do not overlap as infrared energy is projected over the belt. Thus, the minimum distance between the heating elements on the conveyor must be at least equal to or greater than the spacing between the individual heating elements. A heating element that is too far from the conveyor belt will require a relatively high amount of energy to achieve the product temperature at a given wavelength due to the fact that the energy density decreases as the square of the distance between the heating element and the carrier.
[000197] The watts density of a heating element can be expressed in watts per inch of the length of the heating element. If the wattage density of a heating element is too high, then the heating elements will need to be located very far from the belt to maintain a heater temperature in order to emit the desired wavelength for a given product temperature. If the wattage density of a heating element is too low, then the heating element may need to be very close to the belt, creating hot and cold spots and / or the heating element may not reach the required heater temperature to achieve the desired wavelength. In order to take into account changes in the moisture content of the product during drying, the heater density of the heater and the spacing between the individual heating elements can be selected based on the predicted moisture content range in a specific zone, and the required wattage expected based on the thermal capacity of the product (Q = mCp (T1-T2)) as well as the amount of water vapor produced (2324.4 J / g (1000 BTU / lb.) of steam).
[000198] Quartz heaters can be transparent or matte and can include a reflector directly on the element or some distance behind the element. For example, each heater support 302, 304, 306, 308 (Figure 6) can include a reflector (e.g., a metal container) positioned behind the heating elements supported by the heater support. Heating elements with a reflector on the element itself will have a relatively higher element temperature under the same conditions due to the reflection of the background infrared directly back to the element itself, resulting in a higher temperature and a shorter wavelength. in the same power setting compared to a heating element that has a reflector that is positioned below the heating element. If the reflector is below the heating element, more of the initial infrared waves can be reflected around the element. The advantage of reflecting around the element is that there may be a more uniform distribution of infrared over the belt, especially in an area where the heating elements are relatively close to the belt due to the high rate of water removal (high heat of vaporization) ). On the other hand, reflectors on the heating elements would be more favorable in control zones where the heaters need to be relatively farther from the belt in order to reduce the maximum distance of the heating elements from the belt, thereby reducing the amount of energy required to achieve the desired wavelength.
[000199] The selection of heater adjustment range, watt density, heater spacing, and reflector configuration can be further explained with reference to Figure 22. Figure 22 shows a schematic illustration of a dryer 500 for drying fruit liquids and vegetables (although this can be used to dry other substances). The dryer 500 comprises five main dryer sections 502, 504, 506, 508, and 510. Each dryer section can include one or more control zones. Typically, each control zone comprises a plurality of infrared heating elements (also referred to as infrared emitters or infrared lamps). Within each dryer section, there may be movable heater supports (for example, 302, 304, 306, 308) that support the heating elements of a control zone, heater supports that support the heating elements of more than one control zone, or a combination of heater supports that support the heating elements of a control zone and heater supports that support the heating elements of more than one control zone. The length of the control zones (in the direction of movement of the conveyor as well as the length of the movable heater supports can vary over the length of the dryer, for example, between 304.8 mm and 3048 mm (1 foot and 10 feet). Generally speaking, shorter control zones and shorter heater supports can provide more precise control over the temperature of the product and can be more responsive to changes in the thermal properties of the product due to moisture loss. dryer 502 extends approximately 10% of the total dryer length; the second dryer section 504 extends approximately 25% of the total dryer length; the third dryer section 506 extends approximately 35% of the total dryer length; the fourth dryer section 508 extends approximately 20% of the total dryer length, and the fifth dryer section 510 extends approximately 10% of the total dryer length.
[000200] The first dryer section 502 is a "lift" section of the dryer in which the product temperature is increased in a short amount of time to an optimum temperature for more efficient evaporation for the product. In this dryer section, the control zones can be relatively short to increase the product temperature as quickly as possible while preventing overheating. In specific embodiments the watts density of the heating elements in this dryer section is in the range of approximately 0.78-3.14 watts / mm (20-80 watts / inch) with 1.96 watts / mm (50 watts / inch) ) being a specific example. The heater spacing (the distance between the individual heating elements is in the range of approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), with 50.8 mm (2.0 in) being a specific example.The length of each control zone is in the range of approximately 152.4 mm (6 in) to approximately 1524 mm (60 in), with 762 mm (30 in) being a specific example (each zone having approximately 15 heating elements.) The length of each mobile heater bracket ranges from approximately 152.4 mm (6 in) to approximately 1524 mm (60 in), with 762 mm (30 in) being a specific example. each movable heater support can support the heating elements of a control zone (as shown in Figure 6) the distance between the heating elements and the conveyor 230 within the first drying section 502 can be adjusted between approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), 50.8 mm (2.0 in) with a specific operating distance. The reflectors mounted below the heating elements can be used in this dryer section.
[000201] The second dryer section 504 is a high evaporation section of the dryer in which the moisture content is initially high, and the product is kept at an efficient temperature for moisture evaporation. In this section, the process is generally in a stable state, evaporating a large amount of moisture with little effect on the product temperature. Consequently, the control zones can be relatively longer in this dryer section. A relatively large amount of energy is required in this dryer section. In specific embodiments, the watts density of the heating elements in this dryer section is in the range of approximately 0.78-3.14 watts / mm (20-80 watts / inch) with 2.36 watts / mm (60 watts / mm) in) being a specific example. The heater spacing (the distance between the individual heating elements is in the range of approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), with 50.8 mm (2.0 in) being a specific example. The length of each control zone is in the range of approximately 381 mm (15 in) to approximately 6046 mm (240 in), with 3048 mm (120 in) being a specific example. In a specific implementation, each movable heater support can support the heating elements of two control zones.The distance between the heating elements and the conveyor 230 within the second drying section 504 can be adjusted between approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), with 50.8 mm (2.0 in) being a specific operating distance The reflectors mounted below the heating elements can be used in this dryer section.
[000202] The third dryer section 506 is a transition section in which the product transitions to a mainly dry state and becomes very sensitive to heat. Consequently, the lengths of the control zones are desirably relatively shorter in this dryer section to respond to any fluctuations in product characteristics that affect the drying rate. In specific embodiments, the watts density of the heating elements in this dryer section is in the range of approximately 0.78-2.36 watts / mm (20-60 watts / inch) with 1.18 watts / mm 30 watts / inch ) being a specific example. The heater spacing (the distance between the individual heating elements is in the range of approximately 12.7 mm (0.5 in) to approximately 609.6 mm (24 in), with 76.2 mm (3.0 in) being a specific example. The length of each control zone is in the range of approximately 381 mm (15 in) to approximately 3048 mm (120 in), with 762 mm (30 in) being a specific example (each zone having approximately 10 elements The length of each mobile heater bracket is in the range of approximately 381 mm (15 in) to approximately 6096 mm (240 in), with 762 mm (30 in) being a specific example. mobile heater can support the heating elements of a control zone.The distance between the heating elements and the conveyor 230 within the third drying section 506 can be adjusted between approximately 12.7 mm (0.5 in) to approximately 609 , 6 mm (24 in), and more specifically and between approximately 101.6 mm (4.0 in) to approximately 254 mm (10 in). In this drying section, a combination of reflectors mounted below the heating elements and heating elements that have integral reflectors can be used.
[000203] The fourth drying section 508 is a final drying section where the product is primarily dry the control zones are relatively longer to remove the last moisture from the product under relatively stable conditions. Longer control zones are desirable to maintain substantially constant drying. In specific embodiments, the watts density of the heating elements in this dryer section is in the range of approximately 0.78-3.14 watts / mm (20-80 watts / inch) with 2.36 watts / mm (60 watts / mm) in) being a specific example. The heater spacing (the distance between the individual heating elements is in the range of approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), with 101.6 mm (4.0 in) being a specific example.The length of each control zone is in the range of approximately 1524 mm (60 in) to approximately 3048 mm (120 in), with 2286 mm (90 in) being a specific example (each zone having approximately 22 elements The length of each mobile heater bracket is in the range of approximately 381 mm (15 in) to approximately 6096 mm (240 in), with 3048 mm (120 in) being a specific example. mobile heater supports can support the heating elements of a control zone while other mobile heater supports can support the heating elements of two control zones The distance between the heating elements and the conveyor 230 within the fourth drying section 508 can be adjusted between approximately 12.7 mm (0.5 in) to approximately 508 mm (20.0 in), with 406.4 mm (16 in) being a specific operating distance. Heating elements that have integral reflectors can be used in this drying section.
[000204] The fifth drying section 510 is an exit or "decrease" section where the control zones can be relatively short to reduce the temperature of the product for annealing and / or to prevent overheating in a product specifically sensitive to heat. In specific embodiments, the watts density of the heating elements in this dryer section is approximately 0.39 watts / mm (10 watts / inch). The heater spacing (the distance between the individual heating elements is in the range of approximately 12.7 mm (0.5 in) to approximately 127 mm (5.0 in), with 76.2 mm (3.0 in) being a specific example.The length of each control zone is in the range of approximately 1524 mm (60 in) to approximately 3048 mm (120 in), with 762 mm (30 in) being a specific example (each zone having approximately 10 elements The length of each mobile heater bracket is in the range of approximately 381 mm (15 in) to approximately 3048 mm (120 in), with 762 mm (30 in) being a specific example. mobile heater can support the heating elements of a control zone.The distance between the heating elements and the conveyor 230 within the fifth drying section 510 can be adjusted between approximately 12.7 mm (0.5 in) to approximately 381 mm (15.0 in), with 254 mm (10 in) being a specific operating distance. Heating elements that have integral reflectors can be used in this drying section.
[000205] In a specific implementation, a dryer 500 has a total length of approximately 30.4 m (100 feet). The first dryer section 502 has four control zones, each of which is approximately 762 mm (30 in) long and mounted on a respective mobile heater support. The second dryer section 504 has five control zones, each of which is approximately 1524 mm (60 in) long, and ten movable heater brackets, each supporting two control zones. The third dryer section 506 has fourteen control zones, each of which is approximately 762 mm (30 in) long and is mounted on a respective mobile heater support. The fourth dryer section 508 has three control zones, each of which is approximately 2286 mm (90 in) long. The fourth dryer section 508 may include mobile dryer holders that support a control zone and dryer holders that support more than one control zone. The fifth dryer section 510 has four control zones, each of which is approximately 762 mm (30 in) long and mounted on a respective mobile heater support.
[000206] In view of the many possible modalities to which the principles of the described invention can be applied, it should be recognized that the illustrated modalities are only preferred examples of the invention and should not be taken to limit the scope of the invention. Rather, the scope of the invention is defined by the following claims. Therefore, we claim as our invention everything that falls within the scope and spirit of these claims.

权利要求:
Claims (16)
[0001]
A drying apparatus (100, 200), comprising: a mobile product conveyor (230) having a product support surface (231) for supporting a product to be dried; at least one first and a second heater bracket (304, 306), each heater bracket (304, 306) supporting one or more dry radiant heating elements (261, 262) and being mobile with respect to each other and in relation to the conveyor (230) to adjust the distance between each heater support (304, 306) and the conveyor (230); the product conveyor (230) being configured to move with respect to the first and second heater supports (304, 306) so that the product supported on the conveyor (230) is successively heated by the heating elements (261) of the first heater support (304) and the heating elements (262) of the second heater support (306); and a controller (150, 250), characterized by the fact that: said controller (150, 250) is configured to continuously monitor the wavelength of the heating elements (261, 262) and the temperature of the product and adjust the temperature of the heating elements (261, 262) of each heater support (304, 306) and the distance between the heating elements (261, 262) of each heater support (304, 306) and the conveyor (230) so that the heating elements (261, 262) emit radiant heat at a predetermined wavelength and heat the product according to a predetermined product temperature profile as the product is moved through the drying apparatus (100, 200) by product conveyor (230).
[0002]
Drying apparatus according to claim 1, characterized in that the controller (250) comprises at least one first phase angle control device (233) that controls the temperature of the heating elements (261) of the first heater support (304) and a second phase angle control device (233) that controls the temperature of the heating elements (262) of the second heater support (306).
[0003]
Drying apparatus according to claim 1, characterized by the fact that each heater support (304, 306) is supported by a plurality of vertical support posts (310) and is movable up and down in relation to the support posts (310) and each heater support (304, 306) comprises at least one drive mechanism (316, 318, 320) that causes the heater support (304, 306) to move up and down in with respect to the support posts (310).
[0004]
Drying apparatus according to claim 1, characterized in that the heater supports (304, 306) are located below the product support surface (231) and are movable up and down in the direction and away of the product support surface (231).
[0005]
Drying apparatus according to claim 1, characterized in that the controller (250) is configured to adjust the temperature of the heating elements of each heater support (304, 306) and the distance between the heating elements (261, 262) of each heater support (304, 306) and the conveyor (230) so that the product absorbs radiant heat at a substantially constant wavelength as it is carried through the heating elements (261, 262 ) of the first and second heater supports (304, 306).
[0006]
Drying apparatus according to claim 1, characterized in that it also comprises a plurality of temperature sensors (314) positioned to measure the temperature of the heating elements (261, 262) of each heater support (304, 306 ), the controller (250) being in communication with the temperature sensors (314) and being configured to determine the wavelength of radiant heat emitted by the heating elements based on their temperature.
[0007]
7. Drying apparatus according to claim 1, characterized by the fact that it also comprises a plurality of temperature sensors (281, 282) positioned to measure the temperature of the product being heated by the heating elements (261, 262), the controller (250) being in communication with the temperature sensors (281, 282) and being configured to adjust the temperature of the heating elements (261, 262) based on the return of the temperature sensors (281, 282) to maintain the predetermined product temperature profile.
[0008]
8. Method of drying a product, comprising the steps of: applying a product to be dried on a product support surface (231) and a mobile conveyor (230); transporting the product on the conveyor (230) through at least a first heating zone (Z1) and a second heating zone (Z2); and heating the product with a first set of one or more dry radiant heating elements (261) in the first heating zone (Z1) and heating the product with a second set of one or more dry radiant heating elements (262) in the second heating zone (Z2); characterized by the fact that it also comprises: as the conveyor (230) transports the product through the first and second heating zones (Z1, Z2), continuously monitoring the wavelength of the heating elements (261, 262) and the temperature of the product and adjust the temperature of the heating elements (261, 262) and the distance between each set of heating elements (261, 262) and the product support surface (231) to heat the product to a predetermined temperature profile and causing the heating elements (261, 262) to emit radiant heat at a predetermined wavelength.
[0009]
Method according to claim 8, characterized in that the heating elements (261, 262) are located below the product support surface (231) and the act of adjusting the distance between each set of heating elements (261, 262) and the product support surface (231) comprises moving each set of heating elements (261, 262) up and down relative to the product support surface (231).
[0010]
Method according to claim 8, characterized in that the temperature of the heating elements (261, 262) and the distance between each set of heating elements (261, 262) and the product support surface (231 ) are adjusted to maintain a substantially constant product temperature in the first and second heating zones (Z1, Z2) and so that the wavelength of radiant heat emitted in the first and second heating zones (Z1, Z2) is substantially constant.
[0011]
Method according to claim 8, characterized in that the temperature of the heating elements (261, 262) and the distance between each set of heating elements (261, 262) and the product support surface (231 ) are adjusted so that the product temperature in the second heating zone (Z2) is greater than in the first heating zone (Z1) and so that a radiant heat wavelength emitted in the first and second heating zones (Z1, Z2) is substantially constant.
[0012]
12. Method according to claim 8, characterized in that the heating elements (261, 262) in the first and second heating zones emit an infrared radiation of approximately 3 μm.
[0013]
13. Method according to claim 8, characterized in that the heating elements (261, 262) in the first and second heating zones emit an infrared radiation of approximately 6.2 μm.
[0014]
14. Method according to claim 8, characterized in that it also comprises measuring the temperature of the product in the first and second heating zones (Z1, Z2), determining the wavelength of the radiant heat emitted by the heating elements (261 , 262) in the first and second heating zones (Z1, Z2), and adjust the temperature of the heating elements (261, 262) and the distance between each set of heating elements (261, 262) and the support surface of product (2310 based on the measured temperatures and the wavelengths determined in order to heat the product at the predetermined temperature profile and cause the heating elements (261, 262) to emit radiant heat at the predetermined wavelength.
[0015]
15. Method according to claim 14, characterized in that determining the wavelength of the radiant heat emitted by the heating elements in the first and second heating zones (Z1, Z2) comprises measuring the temperature of the heating elements ( 261, 262) in the first and second heating zones (Z1, Z2) and determine the wavelength of the radiant heat in the first and second heating zones (Z1, Z2) based on the measured temperatures of the heating elements (261 , 262).
[0016]
16. Method according to claim 8, characterized in that the product comprises a fruit or vegetable liquid and the act of heating the product substantially dehydrates the fruit or vegetable liquid and the method additionally comprises processing the fruit liquid or dehydrated vegetable in a powder.

类似技术:

---

公开号 | 公开日 | 专利标题

---

BR112013014459B1|2021-04-27|DRYING APPLIANCE AND METHOD OF DRYING A PRODUCT

---

US10281211B2|2019-05-07|Drying apparatus and methods

---

Wang et al.2018|Thermal performance of indirect forced convection solar dryer and kinetics analysis of mango

---

Şevik2013|Design, experimental investigation and analysis of a solar drying system

---

EP0298963B1|1993-08-25|Apparatus for drying fruit pulp and the like

---

Jindarat et al.2011|Analysis of energy consumption in drying process of non-hygroscopic porous packed bed using a combined multi-feed microwave-convective air and continuous belt system |

---

SE527166C2|2006-01-10|Method and apparatus for dehumidification

---

CN104613743B|2016-02-03|The drying unit that a kind of temperature intelligent controls

---

Prommas et al.2012|Energy and exergy analyses in drying process of non-hygroscopic porous packed bed using a combined multi-feed microwave-convective air and continuous belt system |

---

Wray et al.2015|Development of a microwave–vacuum-based dehydration technique for fresh and microwave–osmotic | pretreated whole cranberries |

---

Monteiro et al.2020|Microwave vacuum drying of foods with temperature control by power modulation

---

KR20090077362A|2009-07-15|Near infrared ray drying system and method of controlling the same

---

US9303919B2|2016-04-05|Radio frequency drying of harvested material

---

CN104642415B|2015-12-09|A kind of food drier of automatic control

---

CN104534844A|2015-04-22|Drying device capable of automatically adjusting conveying speed

---

JP6233955B2|2017-11-22|Drying equipment

---

Pavlushin et al.2019|Energy–saving dryer

---

CN104534836A|2015-04-22|Drying device allowing temperature distribution in heating area to be controlled automatically

---

CN104534843A|2015-04-22|Drying device for intelligent preheating area temperature distribution control

---

CN104634083A|2015-05-20|Drying device capable of intelligently controlling temperature

---

RU2587569C2|2016-06-20|Apparatus for drying sugar cubes with microwave radiation

---

Amer2011|MATHEMATICAL MODELING OF TEMPERATURE AND HEAT PROFILES IN PILOT REFRACTANCE WINDOW DRYING SYSTEM

---

GB816794A|1959-07-22|Improvements in or relating to apparatus for drying culture media and the like

---

BR102018004505A2|2019-09-17|SOLAR SIMULATION BENCH WITH UNIFORM IRRADIANCE DISTRIBUTION FOR ENERGY EFFICIENCY TESTS IN PHOTOVOLTAIC PANELS.

同族专利:

---

公开号 | 公开日

---

CA2821114C|2019-01-15|

---

WO2012079094A1|2012-06-14|

---

EP2649391B8|2017-05-31|

---

MX370071B|2019-11-29|

---

CN103348205A|2013-10-09|

---

US20160097591A1|2016-04-07|

---

US20120151790A1|2012-06-21|

---

CL2013001664A1|2014-07-11|

---

ES2632194T3|2017-09-11|

---

EP2649391A1|2013-10-16|

---

US10119760B2|2018-11-06|

---

MX2013006575A|2013-09-13|

---

MX2019014154A|2020-02-07|

---

BR112013014459A2|2016-09-13|

---

EP2649391A4|2015-05-20|

---

PL2649391T3|2017-10-31|

---

CN103348205B|2016-03-23|

---

EP2649391B1|2017-04-12|

---

US9243843B2|2016-01-26|

---

CA2821114A1|2012-06-14|

引用文献:

---

公开号 | 申请日 | 公开日 | 申请人 | 专利标题

---

---

US2400460A|1942-10-01|1946-05-14|Drying & Concentrating Company|Dehydrated edible product and method of obtaining same|

---

US2846319A|1955-07-26|1958-08-05|E J Kelly & Associates Inc|Drying process|

---

US3364587A|1966-03-31|1968-01-23|Leesona Ltd|Movable yarn drier having infrared heaters and automatic controls therefor|

---

US4033263A|1974-12-12|1977-07-05|Harris Corporation|Wide range power control for electric discharge lamp and press using the same|

---

IT8021284V0|1980-03-25|1980-03-25|Argon Service Ltd|INFRARED DRYING OVEN OF THE PERFECT TYPE.|

---

US4631837A|1985-05-31|1986-12-30|Magoon Richard E|Method and apparatus for drying fruit pulp and the like|

---

CN2044339U|1988-09-11|1989-09-13|李双全|Drier for fabric or compound paper cloth|

---

US5037560A|1990-03-09|1991-08-06|Danny Gayman|Sludge treatment process|

---

CN2138280Y|1992-09-16|1993-07-14|天津大学|Plywood heating drier with direction radiation|

---

US5382441A|1993-04-16|1995-01-17|The Pillsbury Company|Method of processing food utilizing infrared radiation|

---

US5557858A|1995-08-25|1996-09-24|Catalytic Industrial Group Inc.|Infrared wood product dryer|

---

US5678323A|1995-11-01|1997-10-21|Domingue; Hille|Apparatus and method for controlled drying of sludge|

---

DE19807643C2|1998-02-23|2000-01-05|Industrieservis Ges Fuer Innov|Method and device for drying a material to be dried on the surface of a rapidly conveyed carrier material, in particular for drying printing inks|

---

JP3735769B2|1998-07-30|2006-01-18|大東製機株式会社|Drying device, drying device assembly and drying method|

---

DE19857045C2|1998-12-10|2001-02-01|Industrieservis Ges Fuer Innov|Coating of objects|

---

US6539645B2|2001-01-09|2003-04-01|Mark Savarese|Drying apparatus and methods|

---

FI20011755A|2001-09-04|2003-03-05|Finnforest Oy|Wood veneer analysis and sorting|

---

KR200265379Y1|2001-10-22|2002-02-25|나눅스|shoes dryer using near infrared rays|

---

US20030150128A1|2002-01-15|2003-08-14|Macaluso Virgil J.|Method for rapid drying of rice and comestible material|

---

CN2604248Y|2003-01-30|2004-02-25|东莞市新力光自动化机电有限公司|Three-dimensional motion control UV lamp solidifying equipment|

---

US7307243B2|2003-05-09|2007-12-11|North Carolina State University|Dynamic radiant food preparation methods and systems|

---

WO2005015102A2|2003-07-24|2005-02-17|Eisenmann Maschinenbau Gmbh & Co. Kg|Device for hardening the coating of an object, consisting of a material that hardens under electromagnetic radiation, more particularly an uv paint or a thermally hardening paint|

---

JP2005215024A|2004-01-27|2005-08-11|Fuji Photo Film Co Ltd|Drying apparatus and drying method|

---

KR100990855B1|2008-01-11|2010-10-29|얼라이드레이테크놀로지 주식회사|near infrared ray Drying system and method of controlling the same|

---

US8819958B2|2010-11-08|2014-09-02|Whirlpool Corporation|End of cycle detection for a laundry treating appliance|AU2013207767B2|2012-01-11|2016-03-10|Columbia Phytotechnology, Llc|Dehydrated plant-derived products and methods for making the same|

---

US10800561B2|2012-01-20|2020-10-13|Koffeefruit Pte. Ltd.|Preparation of coffee-based extracts and powders|

---

CN102854794A|2012-08-14|2013-01-02|王兆进|Intelligent medium-short wave infrared drying equipment controller|

---

US9945610B2|2012-10-19|2018-04-17|Nike, Inc.|Energy efficient infrared oven|

---

JP6227131B2|2013-07-04|2017-11-08|エーファウ・グループ・エー・タルナー・ゲーエムベーハー|Method and apparatus for treating substrate surface|

---

CN104841624B|2015-05-29|2017-05-17|广州卓迅包装机械有限公司|Heating oven|

---

CR20180193A|2015-09-04|2019-03-13|Koffeefruit Pte Ltd|PREPARATION OF COFFEE FRUIT EXTRACTS AND POWDERS|

---

CN105627964A|2016-01-20|2016-06-01|四川大学|Sound field enhanced air flow drying and boundary layer measurement integration experiment system|

---

CN105698519A|2016-03-05|2016-06-22|何朝武|Drying system with voice prompt function|

---

DE102016122965A1|2016-11-29|2018-05-30|Autefa Solutions Germany Gmbh|Textile fiber drying|

---

US10813383B2|2016-12-12|2020-10-27|R.J. Reynolds Tobacco Company|Dehydration of tobacco and tobacco-derived materials|

---

ES2684047B1|2017-02-28|2019-07-05|Xilex Dev S L|POLYMER GRANZA DEHUMECTATION PROCEDURE FOR PLASTIC INJECTION AND EXTRUSION|

---

CN107212531A|2017-07-28|2017-09-29|王文平|A kind of working plate that there is LED to heat for being used in shoe making apparatus|

---

CN108121313A|2017-12-26|2018-06-05|安徽省东乾食品有限公司|A kind of dehydrated vegetables flow line production control system|

---

CN108121265A|2017-12-26|2018-06-05|安徽省东乾食品有限公司|A kind of dehydrated vegetables monitoring method|

---

RU190650U1|2019-03-04|2019-07-08|Федеральное государственное бюджетное учреждение науки "Научно-исследовательский институт сельского хозяйства Крыма"|DRYING DEVICE|

---

RU193685U1|2019-03-20|2019-11-11|Федеральное государственное бюджетное учреждение науки "Научно-исследовательский институт сельского хозяйства Крыма"|DEVICE FOR PULSE INFRARED DRYING OF THERMOLABLE MATERIALS|

---

WO2021207159A1|2020-04-08|2021-10-14|Oregon Drytech, Llc|Drying apparatus|

法律状态:
2018-12-18| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

---

2019-12-03| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

---

2020-08-11| B06A| Notification to applicant to reply to the report for non-patentability or inadequacy of the application [chapter 6.1 patent gazette]|

---

2021-03-16| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

---

2021-04-27| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 12/12/2011, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

---

申请号 | 申请日 | 专利标题

---

US42207610P| true| 2010-12-10|2010-12-10|

---

US61/422,076|2010-12-10|

---

PCT/US2011/064498|WO2012079094A1|2010-12-10|2011-12-12|Drying apparatus and methods|

---